Slurry Injection System And Method For Operating The Same

ABSTRACT

A slurry injection system includes low and high pressure clear fluid manifolds. Low pressure clear fluid is pressurized and communicated to high pressure manifold. A blender unit communicates slurry through a sensor system that generates a flow rate signal and a density signal of the low pressure slurry. The slurry pressurizer is in fluid communication with the high pressure clear fluid manifold through a bypass pump, a mixer, the blender unit and the low pressure clear fluid manifold. The slurry pressurizer forms high pressure slurry that is communicated to the mixer and communicates fluid to the low pressure clear fluid manifold. The mixer mixes the high pressure slurry and high pressure clear fluid from the high pressure clear fluid manifold to form a mixture that is communicated to a slurry injection site. A controller controls the bypass pump using the flow rate and density to control a density of slurry.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a continuation-in-part of application Ser. No. 16/199,675 filed on Nov. 26, 2018, which is a continuation-in-part of application Ser. No. 15/927,345, filed on Mar. 21, 2018 which is a continuation-in-part of application Ser. No. 15/888,133, filed Feb. 5, 2018, which is a non-provisional application of provisional application 62/457,447, filed Feb. 10, 2017, the disclosure of which is incorporated by reference herein. This application also relates to U.S. application Ser. No. 15/888,140 filed Feb. 5, 2018 and U.S. application Ser. No. 15/888,154 filed Feb. 5, 2018.

TECHNICAL FIELD

The present disclosure relates generally to a slurry injection system, and, more specifically, to a method and system for pressurizing concentrated slurry for use in a continuous injection process.

BACKGROUND

The statements in this section merely provide background information related to the present disclosure and may not constitute prior art.

Pumping of process fluids are used in many industries Process fluids may be pumped with various types of pumps such as centrifugal, positive displacement or use of a pressurized drive fluid acting upon the process fluid. A slurry is one type of process fluid used in a process. Slurries are typically abrasive in nature. Slurry pumps are used in many industries to provide the slurry into the process. Sand injection for hydraulic fracturing (fracking), high pressure coal slurry pipelines, mining, mineral processing, aggregate processing, and power generation all use slurry pumps. All of these industries are extremely cost competitive. A slurry pump must be reliable and durable to reduce the amount of down time for the various processes.

Hydraulic fracturing of gas and oil bearing formations requires high pressures typically up to 15,000 psi (103421 kPa) with flow rates up to 500 gallons per minute (1892 liters per minute). The total flow rate using multiple pumps may exceed 5,000 gallons per minute (18927 liters per minute).

Slurry pumps are subject to severe wear because of the abrasive nature of the slurry. Typically, slurry pumps display poor reliability, and therefore must be repaired or replaced often. This increases the overall process costs. It is desirable to reduce the overall process costs and increase the reliability of a slurry pump.

Other components of the hydraulic fracking system also have weaknesses due to the abrasive slurries travelling therethrough. Check valves, pipes, pipe joints and fittings can suffer rapid erosion and “wire drawing” caused by high velocity fluid. Further, pressure vessels may be used and if a large number of penetrations in the tanks are used, those places are also subject to cracking failure from stress concentrations and metal fatigue.

SUMMARY

The present disclosure is directed to an elongated tank that is used in a system injecting abrasive slurries into a very high-pressure process stream with minimal wear on the system components. The system provides high reliability due to the reduced amount of wear.

In one aspect of the disclosure, an elongated tank for a slurry injection system has a side wall disposed in a vertical direction and top wall. The tank further comprises an end cap coupled to the side wall comprising a slurry injection channel and defining a bottom surface of the tank. The bottom side is angled downward from the side wall toward the slurring injection channel.

In another aspect of the disclosure, a system for injecting slurry from a slurry source into a slurry injection site comprises a high pressure pump coupled to a water source and a first elongated tank comprising a first end having a first volume and a second end having a second volume. The first volume is separated from the second volume. A first pipe has a first end external to the first elongated tank. The first pipe extends to the first elongated tank so that a second end of the first pipe communicates clear fluid to the first volume. A second elongated tank comprises a first end having a third volume and a second end having a fourth volume, said third volume separated from the fourth volume. A second pipe has a first end external to the second elongated tank. The second pipe extends to the second elongated tank so that a second end of the second pipe communicates clear fluid to the second elongated tank and ends within the third volume. A plurality of slurry valves is fluidically coupled to the first elongated tank and the second elongated tank. The plurality of slurry valves having a first state, a second state and an intermediate state between the first state and the second state. In the first state, the plurality of slurry valves communicates high pressure slurry from the second volume to the slurry injection site and communicates low pressure slurry to the fourth volume. In the second state, the plurality of slurry valves communicates low pressure slurry to the second volume and high pressure slurry from the fourth volume to the slurry injection site. In the intermediate state the plurality of slurry valves communicates high pressure slurry simultaneously from the first elongated tank and the second elongated tank to the slurry injection site. A first clear fluid valve, in the first state, communicates high pressure clear fluid from the high pressure pump to the first volume and, in a second state, communicates high pressure clear fluid to the third volume. A second clear fluid valve, in the first state communicates low pressure clear fluid from the third volume and in the second state communicates low pressure clear fluid from the first volume. A pulsation damper disposed between the high pressure pump and the first clear fluid valve reducing a pressure reduction when the first clear fluid valve changes between the first state and the second state.

In another aspect of the disclosure, a slurry injection system comprises a low pressure clear fluid manifold, a high pressure clear fluid manifold, and a plurality of clear fluid pumps receiving low pressure clear fluid from the low pressure clear fluid manifold, pressurizing the low pressure clear fluid into high pressure clear fluid and communicating the high pressure clear fluid into the high pressure clear fluid manifold. A blender unit has low pressure slurry therein. The blender unit comprises an outlet communicating the low pressure slurry therethrough. A sensor system is coupled to the outlet and generates a flow rate signal of the low pressure slurry and a density signal corresponding to a density of the low pressure slurry. A mixer is in fluid communication with the high pressure clear fluid manifold and a slurry pressurizer. The slurry pressurizer is in fluid communication with the high pressure clear fluid manifold through a bypass pump, the mixer, the blender unit and the low pressure clear fluid manifold. The slurry pressurizer forms high pressure slurry by pressurizing the low pressure slurry from the blender unit using high pressure clear fluid from the high pressure clear fluid manifold and the bypass pump. The slurry pressurizer communicates high pressure slurry to the mixer and communicates low pressure fluid to the low pressure clear fluid manifold. The mixer mixes the high pressure slurry and high pressure clear fluid from the high pressure clear fluid manifold to form a mixture that is communicated to a slurry injection site. A controller, coupled to the bypass pump and the sensor system, controls an operation of the bypass pump in response to the flow rate signal and the density signal to control a density of high pressure slurry.

In yet another aspect of the disclosure, a method of operating a slurry injection system that has a low pressure clear fluid manifold, a high pressure clear fluid manifold, a plurality of clear fluid pumps, a blender unit having an outlet, a mixer, a bypass pump and a slurry pressurizer comprise receiving low pressure clear fluid from the low pressure clear fluid manifold at the plurality of clear fluid pumps; pressurizing the low pressure clear fluid into high pressure clear fluid at the plurality of clear fluid pumps; communicating the high pressure clear fluid into the high pressure clear fluid manifold from the plurality of clear fluid pumps; communicating high pressure clear fluid from the high pressure clear fluid manifold to the mixer; communicating the high pressure clear fluid from the high pressure clear fluid manifold to the slurry pressurizer using a bypass pump; pressurizing, by the slurry pressurizer, low pressure slurry from the blender unit using high pressure clear fluid from the high pressure clear fluid manifold to form high pressure slurry; communicating low pressure fluid from the slurry pressurizer to the low pressure clear fluid manifold; blending, at a mixer, the high pressure slurry with high pressure clear fluid to form a slurry mixture; and communicating the mixture to a slurry injection site. In one aspect of the disclosure, an elongated tank for a slurry injection system has a side wall disposed in a vertical direction and top wall. The tank further comprises an end cap coupled to the side wall comprising a slurry injection channel and defining a bottom surface of the tank. The bottom side is angled downward from the side wall toward the slurring injection channel.

In another aspect of the disclosure, a system for injecting slurry from a slurry source into a slurry injection site comprises a high pressure pump coupled to a water source and a first elongated tank comprising a first end having a first volume and a second end having a second volume. The first volume is separated from the second volume. A first pipe has a first end external to the first elongated tank. The first pipe extends to the first elongated tank so that a second end of the first pipe communicates clear fluid to the first volume. A second elongated tank comprises a first end having a third volume and a second end having a fourth volume, said third volume separated from the fourth volume. A second pipe has a first end external to the second elongated tank. The second pipe extends to the second elongated tank so that a second end of the second pipe communicates clear fluid to the second elongated tank and ends within the third volume. A plurality of slurry valves is fluidically coupled to the first elongated tank and the second elongated tank. The plurality of slurry valves having a first state, a second state and an intermediate state between the first state and the second state. In the first state, the plurality of slurry valves communicates high pressure slurry from the second volume to the slurry injection site and communicates low pressure slurry to the fourth volume. In the second state, the plurality of slurry valves communicates low pressure slurry to the second volume and high pressure slurry from the fourth volume to the slurry injection site. In the intermediate state the plurality of slurry valves communicates high pressure slurry simultaneously from the first elongated tank and the second elongated tank to the slurry injection site. A first clear fluid valve, in the first state, communicates high pressure clear fluid from the high pressure pump to the first volume and, in a second state, communicates high pressure clear fluid to the third volume. A second clear fluid valve, in the first state communicates low pressure clear fluid from the third volume and in the second state communicates low pressure clear fluid from the first volume. A pulsation damper disposed between the high pressure pump and the first clear fluid valve reducing a pressure reduction when the first clear fluid valve changes between the first state and the second state.

In one aspect of the disclosure, an elongated tank for a slurry injection system has a side wall disposed in a vertical direction and top wall. The tank further comprises an end cap coupled to the side wall comprising a slurry injection channel and defining a bottom surface of the tank. The bottom side is angled downward from the side wall toward the slurring injection channel.

In another aspect of the disclosure, a system for injecting slurry from a slurry source into a slurry injection site comprises a high pressure pump coupled to a water source and a first elongated tank comprising a first end having a first volume and a second end having a second volume. The first volume is separated from the second volume. A first pipe has a first end external to the first elongated tank. The first pipe extends to the first elongated tank so that a second end of the first pipe communicates clear fluid to the first volume. A second elongated tank comprises a first end having a third volume and a second end having a fourth volume, said third volume separated from the fourth volume. A second pipe has a first end external to the second elongated tank. The second pipe extends to the second elongated tank so that a second end of the second pipe communicates clear fluid to the second elongated tank and ends within the third volume. A plurality of slurry valves is fluidically coupled to the first elongated tank and the second elongated tank. The plurality of slurry valves having a first state, a second state and an intermediate state between the first state and the second state. In the first state, the plurality of slurry valves communicates high pressure slurry from the second volume to the slurry injection site and communicates low pressure slurry to the fourth volume. In the second state, the plurality of slurry valves communicates low pressure slurry to the second volume and high pressure slurry from the fourth volume to the slurry injection site. In the intermediate state the plurality of slurry valves communicates high pressure slurry simultaneously from the first elongated tank and the second elongated tank to the slurry injection site. A first clear fluid valve, in the first state, communicates high pressure clear fluid from the high pressure pump to the first volume and, in a second state, communicates high pressure clear fluid to the third volume. A second clear fluid valve, in the first state communicates low pressure clear fluid from the third volume and in the second state communicates low pressure clear fluid from the first volume. A pulsation damper disposed between the high pressure pump and the first clear fluid valve reducing a pressure reduction when the first clear fluid valve changes between the first state and the second state.

Further areas of applicability will become apparent from the description provided herein. It should be understood that the description and specific examples are intended for purposes of illustration only and are not intended to limit the scope of the present disclosure.

BRIEF DESCRIPTION OF THE DRAWINGS

The drawings described herein are for illustration purposes only and are not intended to limit the scope of the present disclosure in any way.

FIG. 1A is a schematic view of a slurry injection system according to a first example of the present disclosure.

FIG. 1B is a schematic view of a slurry injection system according to a second example of the present disclosure.

FIG. 1C is a side view of a horizontally disposed tank for use in the slurry injection system.

FIG. 1D is a side view of an alternative configuration of a tank disposed horizontally.

FIG. 1E is a cross-sectional view of the tank of FIG. 1D.

FIG. 1F is an alternative cross-sectional view of the tank of FIG. 1D.

FIG. 1G is a schematic view of a slurry injection system according to a third example of the present disclosure.

FIG. 1H is a cross-sectional view of a piston formed according to the example of FIG. 1G.

FIG. 1I is a schematic of a first example of a one tank system with high pressure clear fluid depressurization.

FIG. 1J is a schematic of a second example of a one tank system without high pressure clear fluid depressurization.

FIG. 1K is a schematic of an alternate two tank slurry injection system.

FIG. 2A is a cross-section of an exemplary three-way valve in a first position.

FIG. 2B is a cross-section of the exemplary three-way valve in a second position.

FIG. 2C is a cross-sectional view of the three way valve in an intermediate position.

FIG. 3A is a second example of an exemplary three-way valve in a first position.

FIG. 3B is a second example of the exemplary three-way valve in a second position.

FIG. 3C is a cross-section of a first example of a two-way switch.

FIG. 3D is a cross-section of a second example of two two-way switches having two housings and a common actuator in a first position.

FIG. 3E is a cross-section of the second example of the two two-way switches of FIG. 3D in a second position.

FIG. 3F is a cross-section of a third example of a two-way switch.

FIG. 3G is a cross-section of a fourth example of two two-way switches having two housings with a common actuator in a first position.

FIG. 3H is a cross-section of a fifth example of the two-way switches of FIG. 3G in a second position.

FIG. 3I is a cross-sectional view of an alternate two-way switch in a closed position having a balance disk.

FIG. 3J is a cross-sectional view of the two-way switch of FIG. 3I in an open position.

FIG. 4A is a first example of a table for the various valve settings used during operation of the example of FIG. 1A.

FIG. 4B is a second example of a table for the various valve settings used during the operation of the example illustrated in FIG. 1B.

FIG. 4C is a third example of a table for the various valve settings corresponding to FIG. 1E.

FIG. 4D is a fourth example of a table for the various valve settings corresponding to FIG. 1K.

FIG. 4E is a plot of cylinder pressure versus time during the operation of FIG. 1K.

FIG. 4F is a plot of high pressure clear water flow of clear fluid versus time during the operation of FIG. 1K.

FIG. 4G is a plot of low pressure clear water flow of clear fluid versus time during the operation of FIG. 1K.

FIG. 5A is a flowchart for a first example of a method for operating the system of FIGS. 1A and 1B.

FIG. 5B is a flowchart for a second example of a method for operating the system of FIG. 1K.

FIG. 6A is a flowchart of a method for switching states between a first tank and a second tank injection slurry of FIGS. 1A and 1B.

FIG. 6B is a flowchart of a method for switching states between a first tank and a second tank injection slurry of FIG. 1K.

FIG. 7A is a timing chart of an injection system for a multiple unit slurry injection system with a dwell time.

FIG. 7B is a timing chart for a single tank slurry injection system.

FIG. 8A is a schematic of a slurry injection system disposed on trailers.

FIG. 8B is an enlarged cross-sectional view of the static mixer of FIG. 8A.

FIG. 8C is a schematic of a second example of a slurry injection system having a bypass pump rather than valves for redirecting the fluid to the slurry pressurizer.

FIG. 8D is a schematic of a third example of a slurry injection system having a slurry pressurizer bypass valve.

FIG. 8E is a schematic view of a fourth example of a slurry injection system having a slurry pressurizer bypass valve disposed close to the input to the trailer.

FIG. 9A is a flowchart of a method for operating the system of FIG. 8A.

FIG. 9B is a flowchart of a method for operating the system of FIG. 8C.

FIG. 9C is a flowchart of a method for operating the system illustrated in FIG. 8D.

FIG. 9D is a flowchart of a method for operating when an emergency condition is detected.

FIG. 9E is a flowchart of a method for operating the system when a failure is detected.

FIG. 10A is a top view of a slurry injection module.

FIG. 10B is a side view of two slurry injection modules of FIG. 10A.

FIG. 10C is a top view of the slurry injection system of FIG. 10B.

FIG. 10D is a side view of the baseplates of the system of FIG. 10C joined together.

FIG. 11A is a schematic view of the two tank slurry injection system of FIG. 1K with a modified tank design.

FIG. 11B is an enlarged portion of the endcap of one of the tanks of the system of FIG. 11A.

FIG. 11C is a top cutaway view of the system of FIGS. 11A and 11B.

FIG. 11D is an enlarged portion of an alternative example of an endcap of one of the tanks suitable for use in the system of FIG. 11A.

FIG. 11E is a first alternate example of the end wall of a tank.

FIG. 11F is a second alternate example of the end wall of a tank.

FIG. 11G is a third alternate example of the end wall of a tank.

FIG. 11H is a fourth alternate example of the end wall of a tank.

FIG. 11I is a fourth alternate example of the end wall of a tank.

FIG. 11J is a fourth alternate example of the end wall of a tank

DETAILED DESCRIPTION

The following description is merely exemplary in nature and is not intended to limit the present disclosure, application, or uses. For purposes of clarity, the same reference numbers will be used in the drawings to identify similar elements. As used herein, the phrase at least one of A, B, and C should be construed to mean a logical (A or B or C), using a non-exclusive logical or. It should be understood that steps within a method may be executed in different order without altering the principles of the present disclosure. The use of the words “low” and “high” are used relative to the pressures suitable for use in fracking. “Low” pressure is suitable for movement of fluids into or out of pipes. “High” pressure is on the order suitable for fracking which is typically thousands of pounds per square inch.

A slurry injection system 10 is illustrated for injecting slurry into a high pressure slurry injection site 12. The injection system 10 may be used alone or in a multi-unit injection system such as the injection system unit 10A illustrated in fluid communication with the injection site 12. The injection systems 10, 10A may be operated using a common controller 20 such as a programmable logic controller (PLC). The controller 20 may be used to control the plurality of valves within the injection system 10 and the injection system 10A based on feedback from sensors such as flow rate sensors 22, 24. The flow rate sensors 22, 24 generate a first flow rate signal and a second flow rate signal.

The injection system 10 is used for injecting slurry from a slurry source such as a slurry tank 30 using a slurry circulation pump 32. The slurry, under low pressure from the circulation pump 32, is communicated to a first tank 40A and a second tank 40B through a low pressure slurry inlet pipe 34. As set forth below, the low pressure slurry is communicated to one tank at a time.

The first tank 40A and the second tank 40B may be cylindrical or elongated in shape and disposed in a vertical or any angle above horizontal manner as is illustrated. As will also be described below, it may be possible that the tanks may be positioned in a horizontal position. The tanks 40A, 40B have respective vertical longitudinal axes 42A, 42B, respectively. The tanks 40A, 40B each have a respective end cap 44A, 44B. The tanks 40A, 40B have respective first ends 46A, 46B and second ends 48A, 48B. The first end 46A of the first tank 40A has a first volume 50 of clear fluid and the second end 48A of the first tank 40A has a second volume 52 of slurry. The second tank 40B has a third volume 54 of clear fluid at the second end 46B and a fourth volume 56 of slurry at the second end 48B. The volumes 50, 52, 54 and 56 vary during the process.

The tanks 40A, 40B each include a longitudinally extending pipe 60A, 60B. The pipes 60A, 60B may be coaxial with the longitudinal axes at 42A, 42B. Each pipe 60A, 60B may extend from outside of the respective end caps 44A, 44B through an opening 62A, 62B. The pipes 60A, 60B extend to the first ends 46A, 46B through the second ends 48A, 46B of the tanks 40A, 40B.

Flow distribution plates 64A, 64B may be disposed at the ends of the pipes 60A, 60B toward the first ends 46A, 46B of the tanks 40A, 40B. The flow distribution plates 64A, 64B distribute incoming clear fluid across the diameter of the tanks to minimize the mixing of clear fluid with the slurry. The flow distribution plates 64A and 64B helps to minimize mixing in systems using high density slurry and low density slurry.

Each tank 40A, 40B is separated by a separation region 68A, 68B. While the region may be a defined area, in a hydraulic fracturing configuration, clear fluid may be separated from slurry naturally due to the less dense nature of the clear fluid. Should some mixing occur, the concentration of the slurry may be compensated for this. In this example, the clear fluid is disposed at the first ends 46A, 46B of the tanks 40A, 40B. The slurry is disposed at the second ends 48A, 48B. The clear fluid may be water, water mixed with chemicals or slurry additives such as ethylene glycol or other types of hydraulic fluid. “Clear”, in this manner, refers to fluid that does not contain a significant amount of the particles of the slurry.

The slurry may contain various types or sizes of sand particles such as small quartz particles. The slurry may also include other types of chemicals to improve the lubrication and movement of the hydraulic fracturing particles therein.

The end caps 44A, 44B are affixed to the tanks 40A, 40B and may include conical portions 70A, 70B, respectively. The conical portions 70A, 70B may have a larger diameter toward the second volumes 52, 56 and taper to a smaller diameter at the bottom or outer end of the end caps 44A, 44B (longitudinally away from the second volumes 52, 56). The end caps 44A, 44B may also include cylindrical portions 72A, 72B that are coupled to a plurality of slurry valves. The plurality of slurry valves may include outlet valves 80A, 80B and inlet valves 82A, 82B. Valves 80A, 80B are used for communicating slurry under high pressure from the tanks 40A, 40B, respectively. In operation, the valves 80A, 80B may alternately communicate slurry from the second ends 48A, 48B of the respective tanks 40A, 40B.

Inlet valves 82A, 82B communicate fluid from the slurry inlet pipe 34 into the respective tanks 40A, 40B. The inlet valves 82A, 82B may operate alternately so that each of the valves 82A, 82B does not operate at the same time.

The valves 80A through 82B may be check valves that operate in the manner described below. That is, in general, one tank is receiving high pressure clear fluid to force high pressure slurry from the tank while the other tank is receiving low pressure slurry and removing low pressure clear fluid therefrom.

The injection site 12 has an injection manifold 94 that is in communication with a pipe 96 that extends from the check valve 80A and a pipe 98 that extends from the check valve 80B.

A plurality of clear fluid valves are used for communicating clear fluid to and from each of the tanks 40A, 40B and are in fluid communication with a high-pressure clear fluid pump 90 and a clear fluid tank 92.

The clear fluid tank 92 supplies clear fluid to the high-pressure pump 90 through pipe 100 and the flow rate sensor 24. A pipe 102 supplies pressurized clear fluid to a three-way valve 110. The three-way valve 110 has an inlet port 110A, a first outlet port 110B and an outlet port 110C. A pipe 112 fluidically communicates fluid from the outlet port 110C to the injection manifold 94 (or pipe 96 which leads to the injection manifold 94). A pipe 114 communicates high pressure clear fluid from the outlet port 110B to a second three-way valve 120. The valves 110 and 120 may be referred to as high pressure valves. A bypass valve 124 may also communicate fluid from the high pressure pump 90 to the pipe 114 through pipe 126. The valve 124 may be a two-way valve used to controllably pressurize port 110B and pipe 114 during changing states. The operation of valve 124 will be described in further detail below. The three-way valve 110 communicates fluid from the inlet port 110A to either the outlet port 110B or the outlet port 110C under control of the controller 20.

The three-way valve 120 selectively communicates high pressure clear fluid from the inlet port 120A to either the first outlet port 120B or the second outlet port 120C. Outlet port 120B is in fluid communication with the pipe 60A through pipe 128. Outlet port 120C is in fluid communication with the pipe 60B through pipe 130. Valve 120 is under control of the controller 20.

A three-way valve 140 is used for selectively communicating low pressure clear fluid from the tanks 40A and 40B under control of the controller 20. In particular, valve 140 has an inlet port 140A in fluid communication with pipe 60A through pipe 142. The valve 140 also has an inlet port 140B in fluid communication with pipe 60B through pipe 144. An outlet port 140C of valve 140 is in fluid communication with the clear fluid tank 92. The fluid from the outlet port 140C is in fluid communication with the flow rate sensor 22 and a two-way flow control valve 146. Both the valves 140 and 146 are controlled by the controller 20. The amount of fluid communicated to the tank 92 may be controlled by selectively controlling the amount of fluid flowing through the valve 146. The fluid communicated through the valves 140 and 146 is under low pressure as will be described in further detail below. The closed inlet port 140A or 140B of valve 140 is under high pressure due to the high pressure slurry operation. A pipe 148 communicates fluid from the valve 146 to the tank 92.

A three-way valve 150 is also in communication with the tanks 40A and 40B. In particular, the valve 150 includes an inlet port 150A in fluid communication with the pipe 60A through pipe 152. Inlet port 150B is in fluid communication with the pipe 60B through pipe 154. Outlet port 150C of valve 150 is in fluid communication with the pipe 148 through pipe 156. The valve 150, as will be described in more detail below, is used for equalization or reduction of the pressure within the tanks 40A, 40B. The valve 150 is used for communicating clear fluid from the first volume 50 and the third volume 54. The valve 150 selectively communicates high pressure clear fluid from either the inlet port 150A or port 150B to the outlet port 150C which ultimately communicates clear fluid through the pipe 156 to the tank 92. The pipe 156 may be directly input into the tank 92 or fluidically coupled to pipe 14B. The valve 150 is used to lower the pressure within the highly pressurized tanks prior to when the state of the valves 110, 120 is changed. Ultimately, the use of the valve 150 helps reduce the overall pressure and thus the effort to switch valves 110 and 120 is lower and potential for valve wear and erosion is reduced.

Pipes 60A and 60B may also be in fluid communication with a respective valve 160A, 160B. The valves 160A and 160B are at the lowest point of the respective pipes 60A, 60B and are used to purge air from the volume within the respective 40A, 40B.

A check valve 170 may also be in communication between the injection manifold 94 and the pump 90. In the illustration, check valve 170 is fluidly coupled between the pipe 102 and the injection manifold 94. The check valve 170 is used for directing the flow from the high pressure pump 90 to the injection manifold during upset conditions such as when the fluid paths, the high pressure valves or pipes associated therewith become blocked or equipment, such as the valves, fail. The check valve 170 may also include a spring 172. The spring 172 keeps check valve 170 closed until the upstream pressure (at the pipe 102) exceeds the downstream pressure (in the pipe 96) by a certain amount.

The valves 110 and 120 may be referred to as high pressure clear fluid valves. Valve 124 may also be included as a high pressure clear fluid valve. Valves 140 and 146 may be referred to as low pressure clear fluid valves. The valve 150 sees a combination of high pressure at the inlet ports 150A, 150B and low pressure at the outlet port 150C. The valve 124 is used for pressurizing the pipe 114 at a certain rate with high pressure clear fluid as will be described in more detail below. Collectively, the valves 110, 120, 124, 140 and 146 may be referred to as clear fluid valves. The plurality of clear fluid valves communicates both high pressure and low pressure fluid to and from the tanks 40A and 40B.

The valves 110, 120 and 140 are capable of handling extreme high pressures such as 15,000 psi (103421 kPa) at flow rates at hundreds of gallons per minute. A sealing force over 50,000 pounds (344737 kPa) may be provided against the valve seat due to an extremely high differential when present. However, the valve 150 may be used to lower the overall pressure during switching. The purpose of valve 110 is to isolate the system by diverting the high-pressure clear fluid flow to the slurry pipe 96 through pipe 112. After system isolation, valve 150 can bleed of residual high pressure thereby placing components of the system at relatively low pressure. The operation of the valves will be described in more detail below. Although the valves are described as “three-way valves” and “two-way valves” and “check valves”, other types of valves may be substituted therein. The three-way valves may be implemented in a plurality of two-way valves. Of course, other types of valves may be substituted from the valves. Check valves may, for example, be two-way valves controlled by the controller 20.

The valves 110, 120, 124, 140, 146 and 150 may be controlled by the controller 20 through the use of electrical signals therefrom. Other valves such as 160A and 160B, although not illustrated in communication with the controller 20, may also be electrically controlled thereby. In addition to electrically, valves 110, 120, 124, 140, 146, 150, 160A and 160B may also operate hydraulically or pneumatically

Referring now to FIG. 1B, an injection system 10′ is illustrated and labeled identically to that of FIG. 1A. The system 10′ illustrated in FIG. 1B operates identically to that set forth in FIG. 1A and may also be part of a multi-unit system. The difference between the systems 10 and 10′ is the three-way valve 150 has been replaced by a pair of two-way valves 210A and 210B for pressure reduction. The two-way valves 210A, 210B are used for communicating high pressure clear fluid to the clear fluid tank 92. The pipe 152 receives clear fluid from the pipe 60A which in turn is communicated through pipe 156 to the clear fluid tank 92. The valve 210B receives clear fluid from the pipe 60B through pipe 154. The valve 210B communicates clear fluid through the pipe 156 to the clear tank 92. For simplicity in overall maintenance and the like, the two-way valves 210A and 210 B may be identical to that of valve 124. That way, maintenance is made easier due to the commonality of parts. The valves 210A and 210B all operate at a high differential and thus may need to be serviced more than the other valves in the system which operate with low pressure differentials between the inputs and the outputs.

The valves 210A and 210B are in electrical communication with the controller 20. That is, the controller 20 may control the opening and closing of the valves 210A, 210B. As will be described in more detail below, the valves may be operated so that either 210A or 210B are open but not both.

Referring now to FIG. 1C, the tank 40A is disposed horizontally. The same reference numerals set forth in FIGS. 1A and 1B are used in FIG. 1C. Because of the higher density of slurry within the tank 40A, the denser slurry will settle toward the bottom of the tank 40A. This results in the clear fluid therein pushing a greater amount of fluid near the top relative to the bottom of the tank in the horizontal direction. As is illustrated, the interface 68A′ is generally at an angle where the top portion is closer to the end cap 44A.

Referring now to FIG. 1D, an alternative example of the horizontal tank 40A is set forth. In this example, a plurality of partitions 180 are used to define a plurality of horizontal channels 182. The partitions 180 help reduce the amount of departure of the interface 68A″ from vertical. In this example, the partitions 180 are formed with a plurality of types that extend in the longitudinal direction. The pipes in this example are cylindrical in shape and have gaps 184 therebetween. The gaps 184 also define horizontal channels within the tank 40A.

In FIG. 1D, the end cap 44A′ is modified to have an enlarged conical portion 70A′. The conical portion 70A′ extends in a horizontal direction so as to be in fluid communication with the horizontal channels 182. That is, the diameter of the conical portion 70A′ adjacent to the channels 182 has been increased. Thus, the conical portion 70A′ redirects slurry both to and from the check valves 82A and 82B.

Referring now to FIG. 1E, a cross-sectional view of one example of the tank 40A is set forth. As can be seen, gaps 184 are disposed between the partitions 180 so that horizontal channels 182 are formed. The partitions 180 are cylindrical in shape and may be formed by pipes. The pipe 60A provides clear fluid to the distributor plate 64A and distributes the clear fluid through the channels 182 and gaps 184 formed by the partitions 180.

Referring now to FIG. 1F, a plurality of partitions are illustrated having radially extending walls 190 that extend from the pipe 60A to the inner wall of the tank 40A. The walls 190 divide the tank into pie-shaped sectors 192. The pie-shaped sectors 192 may be further divided by a concentric wall 194. The concentric wall 194 shares a center point with the tank 40A and the pipe 60A. The walls 190, 194 act as a partition to reduce the amount of displacement of the slurry in an angular manner as illustrated in FIG. 1D.

Referring now to FIGS. 1G and 1H, a slurry injection system 10″ has each of the tanks 40A and 40B with a physical divider between the clear fluid between the first volume 50 and the second volume 52 and between the third volume 54 and the fourth volume 56 rather than the regions 68A, 68B described above. The tank 40A may be disposed horizontally (FIGS. 1A and B), vertically (FIGS. 1C-F) or at angles therebetween. The physical divider may be a piston 220A that has a first opening 222 for receiving the pipe 60A. A piston 220B configured in the same manner may be used in tank 40B around pipe 60B. The piston 220A is loosely fit around the pipe so that the piston 220A can freely travel along the pipe 60A as the pressure of the clear fluid changes. By providing the piston 220A, a more complete separation of the clear fluid and the slurry is provided with less chance of mixing with the slurry. With very high fill and discharge rates, some turbulence may occur and the slurry may mix with the fluid in the configuration of FIGS. 1A and 1B. Further, the tanks 40A, 40B may be oriented in a horizontal position. Providing pistons 220A, 220B also enables the use of the tanks in a horizontal to prevent the mixing of the different fluids within the tank. In tank 40A, the piston 220A is shown in a first position and dotted in a second position. Thus, the piston 220A may move in a longitudinal direction parallel to the longitudinal axis 42A of the tank.

When the piston 220A reaches the end cap 44A, a flap 230 disposed within an opening 232 may open by rotating at the hinge 234. The flap 230 may be a spring-loaded flap and when a sufficient amount of pressure differential is formed between the two sides of the piston 220A, the flap 230 may provide some clear fluid through the opening 232. The hinge 234 may instead be spring-loaded to provide a resistance from the flap 230 opening until the piston 220 reaches the end cap 44A of the tank 40A. The dotted flap illustrates the open position of the flap 230. It may be desirable to allow a small amount of clear fluid from volume 50 to travel through the conical portion 70A into the cylindrical portion 72A and into opening 62A of the end cap 44A so that the clear fluid flows just past check valve 80A and into the pipe 96. The conical shape minimizes flow turbulence of the slurry out of the tanks 40A, 40B. This allows the check valve 80A to close within clear fluid and thus in a cleaner environment. Tank 40B may also be operated in a similar manner in that the clear fluid may transmit through the piston 220B so that the check valve 80B closes in a cleaner environment. The force needed to open the flap 230 by overcoming the spring force may be relatively small. That is, only a few pounds per square inch may be sufficient to open the flap to allow the fluid to flush the check valves 80A or 80B.

Referring now to FIG. 1J, the same reference numerals are used to indicate the same components as FIGS. 1A-1D. In this example, only a single tank 40A is provided with the attached components in the slurry injection 10″'. In this example, the tank 40A may be configured in the same manner as set forth in FIGS. 1A or 1G in that the separation region 68A or the piston 220A (of FIG. 1G and 1H) may be set forth between the first volume 50 and the second volume 52.

One difference between FIGS. 1A-1H and FIG. 1G is the lack of a slurry tank 30 and pump 32. In this example, the check valve 82A is in fluid communication with a low pressure slurry manifold 240. The low pressure slurry manifold 240 may be a common source shared between multiple tanks in a multiple tank type system. Of course, a slurry tank 30 and pump 32 may be in communication with the low pressure slurry manifold 240. Another difference between FIG. 1E and FIGS. 1A-1H is the lack of a high pressure pump 90 and a low pressure fluid tank 92. A low pressure clear fluid manifold 242 is used to receive the low pressure fluid from the port 140A′. A high pressure clear fluid manifold 244 is in communication with the valve 110. Although the pump 90 is not illustrated in this example, a high pressure clear fluid pump may be used somewhere in the system for generating the high pressure within the high pressure clear fluid manifold 244.

In this example, the flow rate sensor 24′ has been modified to be positioned downstream of the valve 110 rather than between the clear fluid tank and the pump as illustrated above. The flow rate sensor has been labeled 24′ to indicate its change of position. However, the flow rate sensor 24′ generates a flow signal corresponding to the amount of flow into the pipe 60A and thus into the tank 40A.

The valves 120 and 140 illustrated above have been changed from three-way valves to two-way valves and are indicated as valve 120′ and 140′. Port 120B′ is in fluid communication with the pipe 60A. Likewise, port 140B′ is also in fluid communication with the pipe 60A. Port 120A′ is in fluid communication with the flow rate sensor 24′, pipe 114 and valve 124 and port 1106 of valve 110.

The slurry injection system 10 ^(IV) may be referred to as an asynchronous system. In the previous figures, the fill rate of given tank is no faster than the discharge rate of the second tank. However, by increasing the fill rate of the slurry, the slurry fill duration can be substantially reduced and the capacity rate to discharge high pressure slurry for each tank is increased.

In operation, the three-way valve 110 communicated fluid from port 110A through 1106. The high pressure fluid enters pipe 114 and flow rate sensor 24′. The valve 120′ communicates fluid from port 120A′ to 120B′ and into the pipe 60A. It is presumed that the tank 40A was previously filled with low pressure slurry. The high pressure clear fluid forces high pressure slurry through check valve 80A and to the injection site 12 through the injection manifold 94. As in a similar manner to that set forth above, when the flow rate sensor 24′ indicates the volume of clear fluid has flushed the slurry from the tank 40A and, if desired, passed check valve 80A, the three-way valve 110 is commanded to divert fluid from port 110A to outlet port 110C. Valve 210A is open which depressurizes the pipe 60A and the tank 40A by communicating fluid to the low pressure clear fluid manifold 242. Valve 120′ is closed and valve 140′ is open under low pressure. Thereafter the valve 210A is closed. Low pressure slurry from the low pressure slurry manifold 240 opens the check valve 82A to allow low pressure slurry to enter the tank 40A and expel clear fluid through the pipe 60A. The clear fluid leaves the tank 40A and pipe 60A through the open valve 140′. The opening and closing of the valves is under the control of the controller 20. The flow rate sensor 22 is used to indirectly determine the amount of slurry that has entered the tank 40A. When the desired amount of slurry as determined by monitoring the flow of clear fluid out of the tank is reached, valve 140′ is closed and valve 120′ is open. The valve 124 is open which directs high pressure clear fluid from the high pressure clear fluid manifold 244 to be communicated to the pipe 114 through the pipe 126. After some pressure is built up in pipe 114, valve 110 communicates high pressure clear fluid from port 110A to port 1106 and valve 124 is closed. High pressure clear fluid then enters the pipe 60A through valve 120′ and check valve 82A is closed and check valve 80A is open.

The valve 170 is configured in a similar manner to that described above relative to the spring 172. That is, the valve 170 may also include a spring 172 in a similar manner to that set forth above. Valve 170 opens when a sufficient force is between the high pressure clear fluid manifold 244 and the pipe 96 or the injection site 12. Again, the valve 170 is open when damage to the valve or other components of the system is present or flow conditions have been upset. The valve 170 should be open when the upstream pressure is about 100 pounds per square inch higher than the downstream pressure. This ensures that the valve will not open during normal operation.

Referring now to FIG. 1J, the same components set forth in FIG. 1E are labeled in the same manner. In this example, the slurry injection system 10 ^(IV) has valves 120′ and 140′ that are presumed to be robust enough to be switched under high pressure. Thus, there is no pressure relief using valves 110 and 124 as in the previous examples. In this example, the flow rate sensor 24′ measures the amount of high pressure clear fluid that is communicated to the pipe 60A through the valve 120′. Valve 140′ is closed. Clear fluid displaces slurry through the check valve 80A. When the amount of slurry through the check valve 80A has reached clear fluid as determined by the flow rate sensor 24′ and thus the volume of fluid, the valve operation is reversed in that valve 120′ is closed while valve 140′ is open. This allows the tank 40A to be depressurized and low pressure slurry is then communicated to the tank to restart the process. When the amount of clear fluid that leaves the tank corresponds to a desired amount of slurry being input to check valve 80A, the valves 120′ and 140′ are reversed in operation.

Referring now to FIG. 1K, a similar example to that set forth in FIG. 1B is set forth. A slurry injection system 10″ has a generally simpler layout. In this example, valves 210A, 210B and piping 152, 154 and 156 have been removed. Likewise, the valve 124, piping 126, and valve 110 have also been removed. Further, the three-way valve 140 has also been removed and replaced by two-way valves 246A and 246B. A first pipe 248A fluidically connects valve 246A and pipe 60A. A pipe 248B connects valves 246A, 246B and the flow meter 22 which ultimately is in fluid communication with the tanks 92. A pipe 246C couples the valve 246B to pipe 60B. The two-way valves 246A, 246B are used as a return path for low pressure clear fluid being returned to the tank 92 through the flow meter 22, valve 146 and pipe 148.

The 3-way valve 120 connects the high pressure pump to either tank 40A or 40B. The moment that the 3-way valve 120 begins to open, fluid begins to flow from the high pressure tank 40A/B to the low pressure tank 40B/A. In a fraction of a second, both tanks 40A/B would be pressurized to a value roughly equal to 50% of the pressure of the pressurized tank before the 3-way valve 120 is fully opened. This is highly desirable because the high pressure pump 90 does not experience as great of a pressure drop during the valve switching process.

By adding a pulsation dampener 245, the residual brief drop in pressure before the high pressure pump 90 can fully pressurize the lower pressure tank 40A/B is reduced. The pulsation dampener 145 is disposed fluidically between the high pressure pump 90 and the three way valve 120. In FIG. 1K the pulsation dampener 245 may be disposed in pipe 120 or pipe 126.

In operation, tank 40A is pressurized to 10,000 psi and 3-way valve 120 begins to open, there will be an immediate flow to tank 40B which was at low pressure. This may be referred to as an intermediate state. Both tank 40A and 40B will quickly reach an equilibrium pressure of about 5,000 psi. HP pump 90 experiences the drop in discharge pressure until pressure in tank 40B builds up to 10,000 psi. At that time check valve 80B would open thus allowing slurry flow to be established. Pulsation dampener 245 would reduce the severity and length of this pressure reduction to a negligible level.

In this example, the pump 90 is in communication with the three-way valve 120 and, in particular, port 120C through pipe 126. As will be described below, the valve 120 may also have an intermediate state between the first state and the second state. That is, the three-way valve 120 typically communicates fluid to either pipe 60A or 60B. However, in the intermediate position, the valve 120 may communicate fluid to both pipes 60A and 60B for a predetermined time period through ports 120A and 120B, respectively. A configuration of the valve 120 is set forth in further detail below in FIG. 2C.

Referring now to FIGS. 2A and 2B, a valve 250 suitable for use as valve 110 or 120 in FIGS. 1A-1C is set forth. The valve 250 has a housing 252 which may be cylindrical in shape. The housing 252 includes an inlet or central port 254, a first outlet port 256 and a second outlet port 258. A pair of valve seats 260, 262 extends from the interior cavity 264 of the housing 252. The valve seat 260 is disposed between the inlet port 254 and the outlet port 258. The valve seat 262 is disposed between the inlet port 254 and the outlet port 256.

An actuator 270 has a rod or spindle 272 which has a first valve disk 274 and a second valve disk 276 fixedly coupled thereto. The valve disk 274 is disposed between the inlet port 254 and the valve seat 262. The valve disk 276 is disposed between the inlet port 254 and the valve seat 260. Packing 280 may be disposed between the spindle 272 and the housing 252 to facilitate longitudinal movement of the spindle 272 and the valve disks 274 and 276 as in the direction illustrated by the arrows 282 and to prevent leakage of fluid from cavity 264. In FIG. 2A, the valve disks 274, 276 and spindle 272 are moved in a longitudinally outward direction away from the actuator 270 so that the fluid flows between the inlet port 254 and the outlet port 258 as illustrated by the path 284. In FIG. 2B, the spindle is moved in the rightmost position toward the actuator 270 so that fluid travels from the inlet port 254 to the outlet port 256.

The actuator 270 may be various types of actuators such as an electrical actuator or a hydraulic actuator. In this example, an electric actuator has been used. The actuator 270 is sized to move the disks 274, 276 so that high pressure flow between the inlet port and one of the outlet ports is provided (once resumed during the state switching process). Further, the path corresponding to FIG. 1A is a high pressure clear fluid path of clear fluid. The other port which is closed is at a low pressure. The low pressure port corresponds to tank 40A or 40B depending on the state of operation. The high pressure input to the housing “pushes” the closed valve disk against the corresponding valve seat to ensure a very high closing force to prevent leakage. Because the high pressures are relieved during the switching process, the actuator is sized to overcome very little force (a little more than the packing places on the spindle 272).

Referring now to FIG. 2C, the valve 250 illustrated above is shown in an intermediate position in which fluid is communicated between both the inlet port 254 and the first outlet port 256 and the second outlet port 258. That is, fluid is communicated from the first inlet port 254 simultaneously to the first outlet port 256 and the second outlet port 258. The amount of fluid or time in the intermediate state is governed by the pressures involved as well as the distance D between the valve disk 274 and the valve disk 276. The distance D and spindle velocity correspond to the duration of the intermediate state.

Referring now to FIGS. 3A and 3B, a valve 250′ is illustrated having the same reference numerals as FIG. 2A and 2B except for the changed components. The valve 250′ illustrated in FIG. 3A and 3B is suitable for use as valve 140 illustrated in FIGS. 1A-1C. In this example, the valve seats 260 and 262 have been changed to valve seats 260′ and 262′. In this example, the valve seats 260′, 262′ are moved closer to the central port 290, which is an outlet port. The valve disks 274 and 276 are moved outboard of the valve seats 260′ and 262′. In this example, the valve 250′ has one outlet port 290 and two inlet ports 292, 294. One of the inlet ports is at low pressure and one is at high pressure during operation. The open port is at low pressure. The high pressure on the valve disk at high pressure forces it in communication with the associated valve seat. For example, in FIG. 3A, valve disk 274 is forced against valve seat 262′. In FIG. 3B, valve disk 276 is forced against valve seat 260′. In FIG. 3A, fluid path 296 communicates fluid from the second tank 40B to the outlet port 290 through fluid path 296. In FIG. 3B, fluid is communicated from tank 40A to outlet port 290 through fluid path 298. In each of the cases of FIGS. 2A-3B, a gap between the valve disks and the valve seats allows fluid to pass therethrough.

Referring now to FIG. 3C, a two-way valve 310 may be used to replace the three-way valves illustrated in FIGS. 1A-1F. That is, more than one two-way valve may be used to replace the three-way valves illustrated in the example set forth above. For a two-tank operation, two two-way valves may be used to replace a three-way valve. The valve 310 may also be used in a one tank solution as valves 120′ or 140′. The valve 310 includes a housing 312 that has an inlet port 314 and an outlet port 316. The housing 312 includes packing 320 through which an actuator rod 322 extends therethrough. The actuator rod 322 includes a valve disk 324 which is moved by an actuator 326 coupled to the rod 322. The valve disk 324 may be displaced against the valve seat 327. When the valve disk 324 contacts the valve seat 327, the valve 310 is sealed and thus no flow from the inlet port 314 to the outlet port 316 takes place. In this example, when each of the three-way valves are replaced with two-way valves, each valve may have an independent actuator 326 to allow independent control. Thus, each two-way valve may have greater freedom in valve timing.

Referring now to FIGS. 3D and 3E, a pair of two-way valves 310 are illustrated coupled to a common actuator 326. The common components of each valve are primed. In FIG. 3D, the right valve 310′ is open while the left valve 310 is closed. In FIG. 3E, the left valve 310 is open and the right valve 310′ is closed. By providing the exact same functionality as a three-way valve, the examples illustrated in FIGS. 3D and 3E may have some manufacturing advantages in resisting very high pressure operations due to the small size of each valve component.

Referring now to FIG. 3F, a two-way valve 330 suitable for draining low pressure fluid from a tank is set forth. In this example, a port 332 is an inlet port within the housing 334. The inlet port 332 communicates fluid to a drain port 336. The housing 334 has packing 340 that receives the actuator spindle 342 coupled to the actuator 344. The spindle 342 moves the valve disk 350 toward or away from the valve seat 352. In FIG. 3F, the valve seat 352 is spaced apart from the valve disk 350 and thus fluid flows between the inlet port 332 and the outlet port 336. As mentioned above relative to FIG. 3C, the actuator 344 may be provided for each valve so that when two two-way valves replace a three-way valve, independent timing and control may be performed by the actuators for each valve.

Referring now to FIGS. 3G and 3H, two valves 330, 330′ may be in communication with a common actuator 344. In FIG. 3G, the left valve 330 is closed and the right valve 330′ is open. The common components of valve 330 are primed in valve 330′. In FIG. 3H, the left valve is open and the right valve is closed. It should be noted that the valve disk 350 is located between the valve port 332 and the valve seat 352. When closed, the high pressure forces the valve disk 350 against the valve seat 352.

Referring now to FIGS. 3I and 3J, a two-way valve 330′ similar to that illustrated in FIG. 3F is set forth. The common components to those set forth in FIG. 3F are labelled the same. The valve 330′ is suitable for use as the two-way valves of FIG. 1K. In this example, the actuator spindle 342 has both a valve disk 350 and a balance disk 360. The balance disk 360 defines a chamber 362 between the balance disk 360 and the housing 334. The chamber 362 may also be partially formed by packing 364. The packing 364 may be an annular layer disposed on a portion of the inner surface of an inner wall of the housing 334. The chamber 362 is disposed on the actuator 344 side of the housing 334. The packing 364, a sealing surface between the balance disk 360 and the housing 334.

The force pushing the valve disk 350 against the valve seat 352 may exceed 50,000 pounds in various applications. The chamber 362 is exposed to the same pressure as inlet 332. A passage 370 that, in this example, is within the housing 334 communicates fluid from the inlet 332 to the chamber 362. By balancing the force upon the disk 350 by the pressure in the chamber 362, the actuator rod 342 essentially only has to overcome the friction force of the packing 364 and seals 376, 378 in the housing 334 to open the valve.

The valve disk 350 may have a diameter 366. The balance disk 360 has a diameter 368. By changing the relative diameters of the balance disk 360 and the valve disk 350, the net force to open or close the valve may be changed. The diameter may be changed to allow the valve 330′ to fail open or fail closed should the actuator 344 malfunction. That is, if the diameter 368 of the balance disk 360 were substantially larger than the diameter 366 of the valve disk 350, the valve 330′ would automatically open if the actuator 344 were to fail. That is, the actuator 344 would need to exert a force toward itself to the keep the valve disk 350 against the valve seat 352. The diameter 366 and 368 may be referred to as a sealing diameter.

The first seal 376 may be disposed adjacent to the actuator spindle 342 and adjacent to the chamber 362. The second seal 378 may also be disposed adjacent to the actuator spindle 342 closer to the actuator 344. The seal 378 may also be disposed within the housing 334. A drain line 380 may be disposed between the first seal 376 and the second seal 378. The drain 380 provides a path of high pressure fluid out of the housing and away from personnel should the seal 376 fail. Seal 378 prevents high pressure fluid from escaping toward the actuator 344.

Referring now to FIG. 3J, the valve 330′ of FIG. 3I is illustrated in the closed position in which the chamber 362 is at a minimum volume.

Referring now to FIG. 4A, a state table illustrated by FIG. 1A illustrating a transition of the valves from a first state to a second state is set forth. The first state “A” corresponds to the tank 40A injecting high pressure slurry into the injection site 12 while high pressure clear fluid is an input to the first tank 40A. At the same time, tank 40B is receiving low pressure slurry from the slurry tank 30 and expelling clear fluid to the fluid tank 92. During the first state illustrated as “A” in FIG. 4A, valve 80A is open, valve 82A is closed, valve 82B is open and valve 80B is closed. Three-way valve 140 is communicating fluid from port 140B to port 140C to the clear fluid tank 92. Valve 120 is communicating clear fluid from port 120A to 120B. Valve 110 is communicating clear fluid from port 110A to port 110B which ultimately communicates fluid through valve 120 and into tank 40A. Valve 124 is closed and valve 146 is partially open.

In the table set forth in FIG. 4A (and 4B), the bolded cells indicate a change in the valve state. Thus, only the bolded cells will be described in the various states A1-A5. To begin the transition to state A′, multiple valve states are changed in sequence. State A1 is achieved by changing the state of the three-way valve 110 to communicate fluid from inlet port 110A to outlet port 110C. The high pressure clear fluid from the pump 90 is diverted to the injection manifold 94. The high pressure clear fluid is no longer directed through the valve 120.

In state A2, the valve 150 is switched from communicating clear fluid from between port 150B and port 150C to communicating clear fluid from between port 150A and port 150C. The switching pressure differential of the valve 150 is reduced since the high pressure fluid is no longer being communicated to tank 40A through valve 120 due to the relief of high pressure clear fluid flowing to the injection manifold 94 through valve 110.

In state A3, the depressurization of the tank 40A results in the check valves 80A, 82A and 82B switching states. That is, valve 80A is closed, valve 82A is open, and valve 82B is closed. Check valve 80B remains closed for this portion of the state change. The three-way valves 140 and 120 are also changed in state. That is, valve 140 switches to communicate clear fluid from port 140A to port 140C. Three-way valve 120 communicates fluid from port 120A to port 120C. Notice, the switching of valves 120 and 140 are performed when low pressures are at all the ports.

In state A4, valve 124 is open which results in the check valve 80B being open. By opening the valve 124, pipe 114 and thus the flow through valve 120 is increased. Port 110B also sees an increased pressure.

In state A5, valve 124 is closed and valve 110 is switched in state to terminate the diversion of high pressure clear fluid from the pump 90 to the injection manifold 94. That is, valve 110 switches states so that clear fluid is communicated between inlet port 110A and outlet port 110B. The switching is performed while both ports 110A and 110B are under a high pressure due to the diversion of high pressure clear fluid through valve 124.

In this example, states A1-A5 are switched 0.20, 0.3, 0.2, 0.25 and 0.20 seconds respectively for a total switching state time of 1.15 seconds. Of course, the timing may be adjusted based on various conditions.

In state A′, a steady state of operation is achieved with check valve 80A closed, check valve 82A open, check valve 82B closed, check valve 80B open, and three-way valve 140 communicating low pressure fluid to the tank 40A. Valve 120 is communicating high pressure clear fluid to the tank 40B which results in high pressure slurry being injected into the injection site 12 through the injection manifold 94. The valve 150 is communicating fluid from tank 40A while valve 124 is closed. Valve 146 is partially open. As will be described in more detail below, the switching of the valves takes place based upon comparison from the signals from the flow rate sensors 22 and 24. A comparison of the flow signals from flow rate sensors 22 and 24 are compared. The flow rate sensor signals correspond to the volume of clear fluid entering one tank and leaving the other tank.

Referring now to FIG. 4B, operation of the injection system 10′ illustrated by FIG. 1B is illustrated. All of the states are the same except for the valve 150 has been replaced by the valves 210A and 210B. In steady state A, valve 210A is closed and valve 210B is open while the remaining valves are the same as in FIG. 4A. In state A1, valves 210A and 210B remain closed and open, respectively. In step A2, valve 210A is open while valve 201B is closed. This allows the pressure in the first tank 40A to be depressurized or relieved of pressure. In the remaining states A3-A5, valve 210A remains open while valve 210B is closed. Likewise, in steady state A′, valves 210A and 210B are open and closed, respectively.

Referring now to FIG. 4C, a state diagram illustrating the operation or position of the valves of FIG. 1I is set forth. In the slurry discharge state, valve 80A is open, valve 82A is closed, valve 120′ is open, valve 140′ is closed, valve 110 is open, valve 124 is closed and valve 140 is closed. Valve 146 is partially closed so that the flow to the low pressure clear fluid source is regulated. The state A illustrated a slurry discharge state in steady state operation. To transition through the process after slurry has been fully discharged as indicated by the output of the flow rate sensors, state A1 operates in the same manner except for valve 110 has diverted flow to the manifold 94. The remaining states are the same. In state A2, valve 80A is closed and valve 140 is open. This allows the tank 40A to be depressurized.

In state A3, valves 82A, 120′ and 140′ are switched states so that valve 82A is open, valve 120′ is closed and valve 140′ is open. In state A′, slurry begins to fill the tank. Slurry fills the tank until a predetermined amount of clear fluid is discharged as determined by the flow rate sensor 22. In state A′-1, the slurry discharge cycle is started by changing the states of valves 120′ to open and 140′ to closed. This stops the slurry fill. In state A′-2, the valve 110 is open. The system then continues in this state which corresponds to state A where slurry is discharged. The process then starts over again.

Referring now to FIG. 4D, the operation of the system illustrated in FIG. 1K is set forth. In state A, in which tank 40A is pumping high pressure slurry and tank 40B is filling with low pressure slurry, check valve 80A is open, check valve 82A is closed, check valve 80B is closed and check valve 82B is open. Three-way valve 120 is communicating high pressure clear fluid to the tank 40A. The two-way valve 246B is returning low pressure clear fluid to the tank 92 and two-way valve 246A is closed. In state A-1, the state of the two-way valve 246B is changed from open to closed. In state A-2, the check valve 80B is closed and the check valve 82B is open. The three-way valve 120 communicates fluid to both tank 40A and tank 40B during the period of switching states. That is, the three-way valve 120 communicates high pressure clear fluid to the first volume of the first tank 40A and the third volume of tank 40B. The other valves remain the same as in state A-1. Both tanks 40A and 40B are providing high pressure fluid to the injection site 12.

In state A′, three-way valve 120 has completed switching, the cylinders are switched and the check valve 80A is closed, check valve 82A is open. Two-way valve 246A is open and two-way valve 246B is closed. In this state, the tank 40B is providing high pressure slurry to the injection site.

Referring now to FIG. 4E, a plot of the tank pressure versus time for the operation set forth in FIG. 4D is set forth. “120SW” refers to the three-way valve switching state or intermediate state between a first state and a second state. The “C” or “0” next to the valve name denotes the valve as closed or open. Within the intermediate state, both tanks are at high pressure. The drain valve for the tank about to be pressurized is closed before the three-way valve 120 switches states. That is, at time period 420, valve 246B is closed, valve 120 switches states and then valve 246A is opened. The tank pressure at tank 2 increases while the pressure within tank 1 decreases during time period 420. At time period 422, valve 246A is closed, then valve 120 switches states and valve 246B is opened thereafter. At time period 422, the pressure within tank 1 increases and tank 2 decreases. It is noted that at the time that the valve 120 switches states, the intermediate time period or intermediate state is illustrated which allows both tank 40A and 40B to communicate high pressure slurry. Time periods 424 and 426 correspond directly to time periods 420 and 422.

Referring now to FIG. 4F, the high pressure flow into both cylinders is illustrated. At time period 420, the high pressure flow from tank 1 is transitioning from a high pressure to a low pressure while the high pressure flow into tank 2 is increasing from a low pressure to a high pressure. A crossing takes place during the intermediate in which switch 120 is switching states. As the high pressure fluid into tank 2 is increasing, the high pressure into tank 1 is decreasing. This causes an approximate balance in the output of the high pressure slurry as illustrated by the total flow line 430. As is illustrated, the total flow 430 is constant throughout the operating of the system.

Referring now to FIG. 4G, the low pressure flow from each cylinder is illustrated. The flow rate is reduced during the change of states in the two-way valves 246A and 246B and stops completely when the three-way valve 120 is in the intermediate state. The average flow reduction during the time span may be about 60% of the full flow. If the average flow is about 600 gallons per minute, the total time to switch states for the valves 120 and 246A and 246B is 0.9 seconds. The flow reduction is about 6 gallons over 0.9 seconds. The volume of the accumulator 249 of FIG. 1K may be about 18 gallons to reduce the flow variation experienced by the pump so that the flow variation is a negligible value. As is illustrated, during the intermediate state, zero low pressure slurry flow takes place during time periods 420, 422, 424 and 426 during the switching portion of switch 120 or the intermediate state.

Referring now to FIG. 5A, a method of operating the system set forth in FIGS. 1A-1H is set forth. In step 510, the second volume 52 is filled with slurry in tank 40A and a first volume 50 is filled with clear fluid. In step 512, a third volume 54 of the second tank is filled with clear fluid which is reduced by filling the fourth volume 56 with slurry from the low pressure slurry tank 30.

In step 514, the plurality of high pressure valves 110 and 120, in particular, communicate high pressure clear fluid from the pump 90 and into the pipe 60A. In response to communicating the high pressure clear fluid, step 516 moves the region 68A toward the end cap (downward in FIG. 1A) and high pressure slurry is communicated through the check valve 80A into the injection manifold 94 and injection.

In step 518, a fourth volume 56 is fluidically coupled to allow the slurry from the slurry pump 32 and slurry tank 30 to increase the fourth volume. In response to increasing the fourth volume, clear fluid is reduced within the third volume which is displaced through the pipe 60B and is fluidically communicated through the valves 140 and 146 into the clear fluid tank 92. In step 522, the fluid flow rate of fluid from the tank 92 is measured by flow rate sensor 24. In step 524, a second fluid flow rate is determined from fluid flowing from the third volume 54 into the tank 92. That is, the amount of clear fluid from the tank 40B communicated to the clear fluid tank 92 is measured. In step 526, the controller 20 compares the first fluid flow rate and the second fluid flow rate. The flow rates correspond to the volumes entering and leaving tank 92. In step 528, the drain valve 146 is controlled in response to comparing so that the flow through the valve 146 is increased or decreased based upon the comparison. Ultimately, the amount of fluid flowing from the second tank may be controlled so that the amount of slurry ready to be injected from the second tank 40B is available when the tank 40A is depleted of slurry. Preferably, while draining the tank 40A of slurry, the amount of clear fluid may extend through the end cap and just past the check valve 80A so that the check valve 80A closes in a clean fluid environment rather than in a slurry environment in step 530. It is desirable to have the tank 40B and thus volume 56 at a process maximum before states Al -A5 of FIGS. 4A and 4B are performed.

In step 532, the plurality of clear fluid valves are controlled to cause tank 40A to depressurize. This takes place in states Al and A2 of FIGS. 4A and 4B.

In step 534, the valves are changed in state in steps A3-A5 so that the second tank 40B is pressurized while tank 40A is depressurized and fills with slurry. The switching process is described below.

Referring now to FIG. 5B, the operation of the system illustrated in FIG. 1K is set forth. Steps 540-544 are the same as steps 510-514 in FIG. 5A. Thus, the description of the operation of these steps is not set forth. In step 546, the step is performed in a similar manner to that set forth in step 516. In step 546, in response to the high pressure clear fluid in the first volume, the region 68A or the piston is moved. High pressure slurry is communicated from the first tank to the injection site. Valve 246A is closed during step 546.

In step 548, the fourth volume is coupled to a low pressure slurry pump and slurry tank to increase the fourth volume. In step 550, in response to step 548, the third volume is reduced and low pressure fluid is displaced through the valve 246B and through valve 146.

In step 552, a first flow rate of clear fluid from the clear fluid tank 92 to the first volume 50 is measured. In step 554, a second fluid flow rate of fluid from the third volume 54 through the valve 246B is measured using the flow meter 22. In step 556, the flow rate or volume of the clear fluids based on the flow rates is compared. In step 556, the drain valve 146 is controlled in response to comparing to increase or reduce the clear fluid from the third volume. In step 560, the optional step of communicating clear fluid past the check valve such as the check valve 80A is set forth.

Referring now to FIG. 6, 6A, the switching of the valves in the states between state A and state A′ is illustrated in flowchart form. In step 610, if the desired amount of clear fluid being removed from the second tank 40B has been reached, the switching process begins. As mentioned above, this corresponds to the flow rate or volume determined by the flow rate. Step 610 uses the comparison of step 526 to make this determination. In step 612, the process of switching from state A to A′ of FIGS. 4A and 4B is set forth. In step 614, high pressure clear fluid is redirected to the injection manifold through the three-way valve 110. In step 616, the first tank 40A is coupled to the clear fluid tank through valve 150. Check valve 80A closes in step 618 when the pressure in the tank 40A is reduced. The pressure reduction may be to or nearing to ambient pressure. In step 620, the state of the three-way valves 150 and 120 are also changed as the valves are changed toward state A′.

In step 622, the pipe to the three-way valve 120 is pressurized by opening the valve 124. In step 624, and in response to the bypass valve 124 being closed, valve 82B is closed and check valve 80B is open. Thereafter, in step 626 the state of the three-way valve 110 is changed to communicate high pressure clear fluid to tank 40B through the three-way valve 120. In step 628, high pressure slurry is discharged from tank 40B. In step 630, the check valve 82A is open to force clear fluid from the tank by displacing the clear fluid with low pressure slurry from the tank 15 and the slurry circulation pump 32. In step 632, clear fluid is communicated to the tank 92 through the valve 140 and valve 146.

Referring now to FIG. 6B, the switching process of FIG. 1K is set forth. FIG. 6B continues the process of FIG. 5B. In step 640, when the programmed amount of clear fluid from the second tank 40B is removed, the switching process begins in step 642. In step 644, valve 246B is closed. In step 646, the three-way valve 120 is placed into an intermediate position so both valves 80A and 80B supply high pressure slurry to the injection site 12. In step 648, the three-way valve 120 continues switching to change state from the first state to the second state through the intermediate state. In step 568, valve 246A is open. When the three-way valve 120 completes switching, tank 40A is no longer communicating high pressure fluid because the high pressure pump is no longer communicating high pressure fluid to the first volume. When valve 246A opens, the pressure is reduced and the check valve 80A is opened in step 642. The three-way valve continues to change state to allow only tank 40B to begin pumping slurry to the injection site 12. In step 656, high pressure slurry is continued to be discharged through the tank 40B. In step 658, the check valve 82A opens to force clear fluid into pipe 60A. In step 660, clear fluid is directed from the clear fluid tank 92 from tank 40A to the two-way valve 246 and valve 146.

Referring now to FIG. 7A, a timing diagram for a multiple unit system is set forth. Each unit referred to in FIG. 7A comprises a pair of tanks. In FIG. 1, only two units are illustrated. However, as mentioned above, a plurality of units are set forth. In this example, five units, unit 1-unit 5, are controlled having staggered starts of two seconds. That is, unit 1 starts at time 0 while unit 2 starts at 2 seconds, unit 3 at 4 seconds, unit 4 at 6 seconds, and unit 5 at 8 seconds. A small dwell time such as one-half second may be used in between each cycle for each unit to accommodate slightly slower cycle rates or other variations. That is, the nominal cycle illustrated in FIG. 7A is 9.5 seconds with a one-half second dwell time therebetween. Unit 1 restarts after the dwell time at 10 seconds, unit 2 at 12 seconds, unit 3 at 14 seconds, unit 4 at 16 seconds and unit 5 at 18 seconds.

By staggering the start times and maintaining such during operation, the amount of slurry injected during the process may be maintained at a constant rate. If the units would be in sync in terms of start times (all start at the same time) this may generate stress in the piping, valves and other components. Preferably, the number of units may equal the cycle time divided by the switching time plus the dwell time which is multiplied by an integer. In this case, the cycle time is 10 seconds divided by the 2 second. The results are 5 units to obtain minimal flow variation. However integer multiples 10, 15 or 20 units (or more) may also be used to minimize flow variation.

Referring now to FIG. 7B, a timing chart of a system is set forth using single tank control such as the single tank of FIGS. 1E and 1F above. Single tank control with rapid slurry charging is set forth in FIG. 7B. In this example, each unit has a nominal five-second cycle time with four-second slurry discharge and a one-second slurry fill. In this example, no dwell time is assumed. However, a dwell time may be used in operation. The ratio of the slurry fill time to the slurry discharge time is 1:5. That is, the discharging of slurry takes place 80% of the time and slurry filling takes place 20% of the time. This is increased over the examples including two tanks in which half the time the tank is charging while the other half of the time the tank is discharging (i.e., 50%). The preferred number of tanks equals the cycle time divided by the slurry fill time in the preceding example, this would be five (5) tanks. In the example set forth in FIG. 7B, based on the aforementioned slurry discharge and fill rates with five (5) tanks, the rate of high pressure slurry output and low pressure slurry input is uniform. In the example set forth in FIG. 7B, the same discharge and fill times are used but in this case, six (6) tanks are used thus the rate of slurry output of the entire system is not uniform. Each of the single tanks will operate in phase for one second of every five seconds. As shown in FIG. 7B, the simultaneous slurry filling of units 1 and 6 happens at the time between four and five seconds, nine and ten seconds, fourteen and fifteen seconds and nineteen and twenty seconds. The amount of high pressure clear fluid used for slurry pressurization drops by one unit of 16.7% for one second every five seconds. Since the high pressure pumps are positive displacement pumps running at a constant speed, the excess flow is diverted by the valve 170 illustrated in FIGS. 1E and 1F. When the tanks are in-phase and thus reducing the flow of high pressure fluid to the tanks, the excess high pressure fluid flow is diverted to the slurry manifold 94 through the check valve 170. The dilution of the slurry caused by the diversion of flow may be accommodated by making the slurry more concentrated. In the present example, a slurry concentration increase of 3.3% is used to accommodate the extra high pressure clear fluid that is bypassed through check valve 170.

Referring now to FIG. 8A, a slurry concentrate pressurizer configuration 810 is illustrated. In this example, clear fluid is provided from a clear fluid source such as a reservoir 812 or tank. The reservoir 812 is in fluid communication with a low pressure pump 814. Clear fluid from the reservoir 812 enters a low pressure clear fluid manifold 816. The low pressure clear fluid manifold 816 is in communication with a trailer 818. Because the systems are moved from wellsite to wellsite, mounting the system components to a trailer is suitable. The trailer 818 may also be referred to as a “missile.” The trailer 818 has a portion of the low pressure clear fluid manifold 820 and a portion of a high pressure clear fluid manifold 822 coupled thereto. The low pressure manifold 820 is in fluid communication with a plurality of high pressure clear fluid pumps 830. The pumps 830 may be referred to as fracking pumps. The plurality of pumps 830 may all be disposed on trailers 832 that may be hooked to a semi for easy transport from fracking site to fracking site. One or more pumps 830 may be disposed on each trailer 832. Each of the pumps 830 draws low pressure fluid from the low pressure manifold 820 through an inlet pipe 840 and discharges high pressure clear fluid through an outlet pipe 842. Only one each of pipes 840 and 842 are labeled. The high pressure manifold 822 is in fluid communication with a static mixer 852 through a two-way valve 850. The static mixer 852 is in communication with a well head 854. The high pressure clear fluid manifold 822 is in fluid communication with a slurry pressurizer 860 through a valve 862. A controller 864 is used to control the valves 850, 862 so that a portion of the high pressure clear fluid transmits through the valve 850 and a portion of the high pressure clear fluid is communicated to the slurry pressurizer 860. The controller 864 may be a programmable logic controller (PLC) that acts in response to one of more flow rate sensors 866A, 866B or 866C. Of course, flow rate sensors 866A, 866B, 866C may be disposed at various locations throughout the system 810 and generate flow signals that the controller 864 uses to control the system.

The slurry pressurizer 860 receives high pressure clear fluid and generates high pressure slurry through an output pipe 870 which is in fluid communication with the static mixer 852. That is, the pipe 870 is in fluid communication with a point between the valve 850 and the static mixer 852. The static mixer 852 forms a mixture of concentrated high pressure slurry from slurry pressurizer 860 and water from the valve 850.

The slurry pressurizer 860 also receives low pressure slurry from a blender unit 872 through a pipe 874. The blender unit 872 may also receive additive from an additive tank 876 which is in fluid communication with a dosing pump 878. The dosing pump 878 communicates the fluid from the additive tank 876 into the blender unit 872. The additive within the additive tank 876 may comprise a gel or other types of additive using in the fracking process. The slurry unit 872 may blend slurry, fluid and additives to form the low pressure slurry.

A centrifugal separator 880 receives low pressure fluid from the slurry pressurizer 860 through pipe 881. The centrifugal separator 880 may separate any residual slurry from within the low pressure discharge and communicate the slurry matter to the blender unit 872 through the pipe 882 for re-use. The separator 880 may also communicate clear fluid to the low pressure manifold through pipe 884.

The blender unit 872 may also receive low pressure clear fluid from the low pressure manifold 816 through a pipe 886. The low pressure clear fluid may be used to form the slurry.

In operation, the slurry pressurizer 860 may be disposed on a trailer 890. The slurry pressurizer unit 860 may be one or more of the examples set forth in FIG. 1A-1F. Both single or double tank slurry injection units may be used for the slurry pressurizer 860. In operation, the controller 864 controls the valve 850. The valve 850 may be used to create a differential pressure between a pipe 892 and pipe 870. The differential pressure may be 75 psi or less. The valve 862 may be precisely controlled so that the pressure thereacross is between 1 and 20 psi. Valve 850 may be designed to not fully close. That is, a predetermined amount of flow through the valve 850 so that a predetermined amount of pressure differential is present across the valve 850. For example, a 100 psi pressure differential may be used. The valve cannot fully close preventing accidental over pressurizing of the pumps and the piping. A suitable valve may be a leaky butterfly valve or a ball valve that is not allowed to physically close due to the geometry therein.

Referring now to FIG. 8B, the static mixer 852 is illustrated in further detail. The static mixer 852 has mixing elements 910 set forth therein for mixing the slurry and clear fluid communicated through the valve 850. The static mixer 852 blends the clear fluid and the concentrated slurry from the slurry pressurizer 860 that is received through the pipe 870.

In the example set forth in FIGS. 8A and 8B, the fracking pumps are supplied by a single low pressure clear fluid line. The slurry pressurizer 860 draws low pressure clear fluid and returns low pressure clear fluid back to the clear fluid manifold 816. These connections minimize the amount of piping in a system. The centrifugal separator 880 separates the slurry particulates from the low pressure clear fluid to negligible amounts so that a minimum amount of particulates are in the clear fluid when entering the high pressure pumps. If various ones of the pumps 830 fail, the system can continue to pressurize slurry with minimal effect on the operation. The trailers 832 containing the pumps 830 may easily be maneuvered to allow additional or replacement pumps to be quickly connected to the trailer 818.

Because of the configuration, all the high pressure slurry mass is provided by the trailer containing the slurry pressurizer 860. The slurry pressurizer 860 may use vertical cylinders which keep the slurry in drive fluid from excessive mixing. As mentioned above, pistons may also be used within the various tanks to prevent mixing of the fluids therein, particularly if the tanks are disposed at another angle other than vertical. The valves within the slurry pressurizer have a generally low cycle rate of once every five to ten seconds versus six times per second in a typical fracking pump. Valves designed for low velocities and materials that minimize erosion from concentrated slurry may be used.

Some slurry processes use 0.5 pounds of sand per gallon of high pressure clear fluid or about 6% concentration by weight. Highly dense slurry may contain five pounds of sand per gallon. Based on the ratio, the slurry pressurizer 860 may only need to handle a flow of approximately 10% of the total high pressure clear fluid flow to achieve a desired slurry concentration downstream of the static mixer 852. The additive tank 876 may pass the additives through the slurry pressurizer 860 and the capacity of the slurry pressurizer may be reduced. Because the slurry pressurizer 860 may provide a highly concentrated slurry due to the later mixing within the static mixer 852, the system may be referred to as a slurry concentrate pressurizer. The slurry pressurizer is capable of handling very high slurry concentrations due to low flow velocities and relatively long cycle times which minimize wear of the check valve. Therefore, the fluid capacity hence the size of the equipment can be relatively small.

Referring now to FIG. 8C, the schematic of FIG. 8A has been modified to remove the valves 850 and 862 and replace the valves with the pump 894. The pump 894 may be referred to as a bypass or transfer pump in which high pressure clear fluid from the high pressure clear fluid manifold 822 is redirected to the slurry pressurizer 860. A variable frequency drive 896 is in communication with the controller 864. The controller 864 controls the variable frequency drive 896 to control the speed of the pump 894 so that a desired amount of high pressure clear fluid is directed to the slurry pressurizer 860. The controller 864 may provide feedback from the flow meters 866A, 866B and 866C. Further, the controller 864 may receive feedback from the flow meters 22 and 24 in the various stages of the slurry pressurizers. One or more flow signals from the flow meters may be used to control the speed of the transfer pump 894. The remaining portions of FIG. 8A that are illustrated in FIG. 8C are not described because the operation is the same. The bypass pump 894 in conjunction with the variable frequency drive 896 develops the necessary boost to achieve the desired flow rate of high pressure slurry from the slurry pressurizer and thus the desired amount of output through the pipe 870 prior to communication with the mixer 852. Although a variable frequency drive 896 is not necessary, by providing the variable frequency drive 896, more precise adjustment of pressure boosting may be provided. The pressure provided by the pump 894 may be between about 40 psi and 100 psi depending on the desired slurry flow rate and the viscosity of the slurry.

The slurry pressurizer 860 is illustrated having a first stage 898A and a second stage 898B. As will be described in more detail below, providing two stages addresses the fact that the amount of proppant in fracking operations may vary widely depending on the type of geological formation and the preferences of the operation. When “slick” water is used, the proppant concentration may be as low as a few percent. Thus, the slurry pressurizer 860 may operate at a proppant concentration of 50% or higher and thus may only need to handle a very small fraction of the total flow. For example, if the final slurry concentration is to be about 5%, the slurry pressurizer unit when operating at 50%, would only need to handle about 10% of the total flow and thus may single stage 898A may be used. However, some fracking operations may be proppant concentrations of 20%-30%. In such cases, the slurry pressurizer may use two stages such as stages 898A and 898B. However, different numbers of stages may also be used. This is described in FIGS. 7A, 7B. The module configuration of the slurry pressurizer may be desirable, but if the slurry pressurizer handles about 50% concentration, the proppant concentration desired at the well head is 25%, then the slurry pressurizer needs to handle about 50% of the flow. By providing a modularized slurry pressure unit, the costs are minimized and thus the proper amount of stages may be used. If a pressurizer fails, a new stage may be easily input into the system.

Referring now to FIG. 8D, FIGS. 8C and 8A are similar in that a separator 880 is used for separating any potential contamination from the low pressure clear fluid from the slurry pressurizer 860. The pipe 881 communicates low pressure clear fluid to the separator 880 where most of the fluid is separated. In the example illustrated in FIG. 8D, a portion of the separated water and the slurry may be communicated through the pipe 882 to the blender unit 872. Under certain conditions, all of the clear fluid may be communicated from the slurry pressurizer 860 to the blender unit 872. In such a case, the separator 880 may be eliminated.

In FIG. 8D, a configuration that is suitable for compensating for emergency or failure detections is set forth.

A first isolation valve 912A is disposed within the pipe 892 between the bypass pump 894 and the high pressure clear fluid manifold 822. A second isolation valve 912B is disposed within the pipe 870 communicating high pressure slurry to the mixer 852.

A bypass pipe 914 is in fluid communication with the pipe 874 and communicates low pressure slurry to the low pressure clear fluid manifold 816 through the valve 916. The valve 916 is normally closed and is operated under various conditions such as an emergency or failure condition or a condition when an amount of slurry produced by the slurry pressurizer 860 is insufficient. Insufficient slurry concentration may be developed most likely at the end of the slurry process where process requirements require the maximum slurry density.

A densometer 918 is also disposed within the pipe 874. The densometer 918 may be referred to as a sensor, a plurality of sensors or a sensor system. The densometer 918 generates a signal corresponding to the density of the slurry from the blender unit 872 within the pipe 874. A flowrate signal may also be generated by the densometer 918. The flowrate signal corresponds to the flowrate of the low pressure slurry that is communicated from the blender unit 872 to the slurry pressurizer 860. By using the flowrate signal and density signal, a constant high density slurry with a predetermined rate of slurry injection into the mixer 852 is used to achieve the desired slurry density flowing to the injection site 854. By changing the pressure from the pump 894, the rate of flow of slurry injection may be changed. The pressure is used to overcome the flow resistance of the slurry through various check valves and the flow resistance of water through the control valves. A very low flow may be obtained with about 0.5 bars pressure boost with flowrates increasing as the change in pressure increases. By using the techniques, about a five to one flow variation may be achieved. Data from the densometer 918 is communicated to the controller 864 through a data line 921A. A data line 921B and 921C are used to control the valve 916 and the pump 894, respectively. Using these techniques, the slurry concentration flowing to the injection site 854 may be varied within a few seconds and thus very precise control of the slurry concentration is obtained. As mentioned briefly above, the concentrated slurry injected at the maximum flowrate may be insufficient to achieve a desired overall concentration. The slurry pressurizer bypass valve 916 may be opened in such conditions to allow some low pressure slurry to flow to the clear water manifold 816. The data line 921B sends a control signal to open the valve 916. The high pressure pumps 830 will thus be exposed to slurry but only for brief periods at a significantly lower concentration than otherwise required. The pressure in line 914 is higher than the pressure in the low pressure clear water manifold 816. Referring now to FIG. 8E, a modification of the valve 916′ is moved closer to the missile 818 and the high pressure pumps 830. Thus, the slurry, which may change in density to meet rapidly changing process requirements, exiting blender 872, through pipe 914′ and circulating through pipe 922, is injected with less delay to missile 818 than in FIG. 8D. In this example, the bypass pipe 914′ is extended so that the valve 916′ is closer to the missile 818. A return line 922 is provided so that a continuous amount of fluid may flow in a loop between the bypass pipe 914′, the return line 922 and the blender unit 872. By providing a continuously circulating amount of slurry, when the valve 916′ opens, the slurry in the pipe 914′ is always at the desired current density thus the correct slurry density will be immediately available to missile 818. The continuous supply of slurry to the well head is provided through the recirculation line 922 in case the slurry pressurizer stops. A flow meter 924 is disposed within the recirculation line 922. The flow meter 924 communicates a flow signal corresponding to the flow of fluid within the recirculation line 922.

Although not illustrated in FIGS. 8D and 8E, flowmeters 866A, 866B and 866C, each coupled to the controller 864 may also be incorporated into the system for monitoring the slurry pressurizer and to allow control of the various components therein.

Referring now to FIG. 9A, a method for operating the system of FIGS. 8A and 8B is set forth. In step 930, clear fluid is received from a tank or reservoir at a low pressure pump. In step 932, the low pressure clear fluid is communicated to a low pressure manifold. The low pressure is not high enough to operate the slurry pressurizer illustrated in FIG. 8A. In step 934, a plurality of clear fluid pumps that are coupled to both a high pressure clear fluid manifold and a low pressure clear fluid manifold increase the pressure of the low pressure clear fluid. In step 936, the high pressure clear fluid generated at the plurality of clear fluid pumps is communicated to a high pressure clear fluid manifold.

In step 938, a portion of the high pressure clear fluid is communicated from the high pressure clear fluid manifold through a static mixer through a first valve. In step 940, a portion of the high pressure clear fluid from the high pressure clear fluid manifold is communicated to a slurry pressurizer through a second valve. In step 942, the flow through the first valve and second valve is adjusted based on a flow rate or a pressure monitored within the system.

In step 944, additives may be added to the low pressure slurry. For example, the additives may be a gel or other types of additives suitable for improving the slurry fracking process. Step 944 is an optional step. Additives may be communicated to a slurry unit from a tank and a dosing pump.

In step 946, low pressure slurry is communicated to the slurry pressurizer. In step 948, high pressure slurry is communicated to the static mixer from the slurry pressurizer. In step 950, the low pressure clear fluid from the slurry pressurizer is communicated to a separator. The low pressure clear fluid is the result of the pressure transfer at the slurry pressurizer of high pressure from the high pressure clear fluid to the increase in pressure of the low pressure slurry to high pressure slurry. In step 952, the slurry residue may be extracted at a separator. The clear fluid may have a small amount of slurry therein. In step 954, the separated slurry at the extractor is communicated to the slurry unit and is later used for reinjecting to the slurry pressurizer. In step 956, low pressure clear fluid is communicated to the low pressure clear fluid manifold from the separator. Should the clear fluid have an acceptably low amount of slurry particles therein, the separator may be eliminated from the system.

Referring now to FIG. 9B, the operation of the system illustrated in FIG. 8C is described in detail. The operation of FIG. 9B is similar to that of FIG. 9A. Steps 958 through 966 are identical to those set forth as steps 930-936 and thus will not be described in greater detail. In step 966, a portion of the high pressure clear fluid is communicated to the blender unit 872 from the clear fluid manifold. In step 940, a portion of the high pressure clear fluid is communicated to a slurry pressurizer through the pump 894. In step 970, the flow through the pump is adjusted based upon the various flow rates. The flow rates from the flow meters 22 and 24 or the flow meters 866A-866B may be used individually or in combination. Steps 972-984 are identical to those set forth as steps 944-956 and thus will not be described in further detail.

Referring now to FIG. 9C a method for operating the system of FIG. 8B is set forth. In step 986 a sensor or sensor system such as the densometer is used to generate a density signal and flow signal of the slurry leaving of the blender unit 872. In step 987 a desired density of the slurry for the injection site is determined at the controller 864.

The speed of the pump 894 is changed to increase or decrease the density of the slurry to well 854 to meet process requirements in step 990. In step 989 if it is determined that the pump is not at maximum capacity (i.e. slurry pressurizer 860 is not at maximum capacity), the system repeats back to step 986. When the slurry pressurizer 860 is at capacity (maximum flow rate) in step 989, step 990 increases the pump speed. After step 988, when the slurry density is to be decreased, step 990 decreases the pump speed. Then, step 994 opens the slurry pressurizer bypass valve 916. Slurry is communicated from the blender outlet 875 to the low pressure clear fluid manifold in step 996. In step 998 slurry is communicated through the high pressure pumps where the slurry is added to the slurry from the slurry pressurizer 860. The slurry density of the slurry injected at the injection site 854 is changed accordingly in step 999.

Another way to control of slurry density entering well 854 is to vary the slurry density exiting blender 872. However, the slurry pressurizer, handling a concentrated slurry, allows another option which is to keep the blender slurry concentration constants but vary the rate of injection into mixer 852 leading to well 854. The later method has a faster response as, with the former method, the relatively large blender tank takes a while to adjust to the desired concentration and then adjusted slurry needs to flow all the way through the array of high pressure pumps 830 and missile 818. By simply changing the rate of slurry concentrate injection from slurry pressurizer via adjustment of speed of pump 892 allows a change in a matter of seconds to well 854. Both methods can be mentioned but the preferred method may be to simply vary the speed of pump 892 in many conditions.

Referring now to FIG. 9D, step 902D determines whether an emergency condition is detected. Step 902D is repeated when an emergency condition is not detected. When an emergency condition is detected in step 902D, the pump 894 is shut down in step 904D. The emergency condition may correspond to a broken pipe within the system. A broken pipe may be detected by one of the flow meters. In step 906D the fracking operation is continued for one more cycle to depressurize the system. In step 908D the system is shut down and the blender unit 872 or the pump 873 therein is depowered.

In step 910D, fracking operations continue for one more cycle to depressurize the pressure in the various parts of the system.

Referring now to FIG. 9E, in step 902E the presence of a failure is determined. When a failure is not detected in step 902E the system continuously monitors step 902E to determine if there is a failure in the system. A failure in the system may correspond to a failure of the slurry pressurizer 960. If a failure is detected in step 902E, step 904E turns off the pump 874. Valve 916 is opened in step 906E. In step 908E, the isolation valves 912A and 912B are closed. In step 910E, fracking operations continue for one more cycle to depressurize the pressure in the various parts of the system.

Referring now to FIG. 10A, a top view of a single stage 1010 corresponding to one of the stages 698A or 698B of FIG. 8C is set forth. In this example, each stage 1010 may be disposed on a baseplate 1012. Each baseplate 1012 may include the first tank 40A, the second tank 40B and one or more valves. In this example, which corresponds to FIG. 1K, the two-way valves 246A and 246B are illustrated together with three-way valve 120. A plurality of pipes is used to interconnect the module 1010 with various other modules and to the injection site and the slurry and clear fluid sources. Pipe 1020 is a low pressure clear fluid pipe. A low pressure slurry pipe 1022 communicates low pressure slurry to the tanks 40A, 40B. A high pressure slurry pipe 1024 communicates high pressure slurry to the injection site that has been pressurized by the tanks 40A and 40B. A high pressure clear fluid pipe 1026 communicates high pressure clear fluid to the tanks 40A, 40B to displace high pressure fluid from the tanks 40A, 40B. Each stage operates according to the manner set forth with respect to FIG. 1K. A first crossover pipe 1030 is fluidically coupled to pipe 1024. A second crossover pipe 1032 is fluidically coupled to pipe 1022.

As is set forth in FIG. 10A, the high pressure pipes 1024 and 1026 are located on one side of the base place 1012 for safety purposes. That is, the high pressure pipes 1024 and 1026 are isolated away from the low pressure pipes 1020, 1022. The low pressure pipes typically require more personnel access.

Referring now to FIG. 10B and 10C, a side view of a first stage 1010 and a second stage 1010′ are illustrated. The base plates 1012 and 1012′ may be joined together using spacer blocks 1040 and pipe couples 1042. The blocks 1040 have the length to allow the installation of the pipe couplings 1042 to connect the various pipes of the various modules.

Referring now to FIG. 10D, the base plates 1012 and 1012′ are illustrated being coupled together by the spacer block 1040. However, the systems are typically used in various non-ideal conditions such as in a field or from a vehicle trailer. Consequently, the base plates 1012, 1012′ may be mounted to an adjustable pad 1050, 1050′. The pads 1050, 1050′ may be coupled to an adjustment bolt 1052, 1052′ that may be turned to change the distance between the pad 1050 and a flange 1054, 1054′, respectively. Thus, the adjustment bolt 1052 provides vertical adjustment for each of the base plates 1012, 1014.

A shoulder bolt 1056, 1056′ is illustrated in a horizontal direction and thus provides horizontal alignment of the spacer 1040 with the base plates 1012, 1056. The shoulder bolts 1056, 1056′ may be coupled to flanges 1058, 1058′ that are mounted to the base plates 1012, 1012′. A drift pin or alignment pin (not shown) may also be used to achieve horizontal alignment prior to installing the shoulder bolts 1056, 1056′.

The first stage 1010 may include a programmable logic controller or controller and thus each additional module may become slaves of the first module using standard electrical interface plugs and connectors. The programmable logic controller or controller may be programmed to handle the necessary number of modules. Preferably, the controller is located at the low pressure side of the base plate 1012 so that the module may be easily reached without being directly adjacent to the high pressure pipes.

Referring now to FIG. 11A, 11B and 11C, the system set forth in FIG. 1K is illustrated having a modified first tank 40A′ and a modified second tank 40B′. During slurry discharge in which water is being emitted to the top of the tank through the flow distribution plate 64A, the slurry may try to settle. Therefore, the tank may be modified to remove the flat bottom portions illustrated in the examples set forth above. As set forth below, a conical or hemispherical end cap may be used at the bottom of the tank that does not induce diffusion during the slurry filling cycle. As will be described in more detail below an angle of the cone of between twenty and thirty degrees may be used to prevent sand from settling but not causing diffusion of the entering slurry flow during the slurry fill cycle.

Tanks 40A′ and 40B′ are illustrated as tanks that are vertically disposed. In this example the tanks 40A′ and 40B′ are modified. In particular, the endcaps 44A′ and 44B′ are modified to reduce the amount of sediment buildup in the bottom of the tank due to gravity. The teaching set forth in FIGS. 11A-11C apply equally to the tanks set forth in FIGS. 1A, 1B, 1G, 1I, and 1J, each of which illustrate vertically disposed tanks. That is, one or both of the tanks 40A′ and 40B′ may be incorporated into one of those systems.

The length of the tank L₁ may be about seven or eight times the inside diameter W₁ of the tank 40A′. This allows the tank enough length for the incoming jet of slurry to dissipate before the slurry reaches the end wall 41.

During slurry discharge in which water is being emitted to the top of the tank through the flow distribution plate 64A, the slurry may try to settle. Therefore, the tank may be modified to remove the flat bottom portions illustrated in the examples set forth above. As set forth below, a conical or hemispherical end cap may be used at the bottom of the tank that does not induce diffusion during the slurry filling cycle. As will be described in more detail below an angle of the cone of between twenty and thirty degrees may be used to prevent sand from settling but not causing diffusion of the entering slurry flow during the slurry fill cycle.

In this example, the endcap 44A′ is modified so that a bottom surface 1120 of the tank is formed between the sidewall 1122 and the slurry injection channel 1110. That is a first edge 1120A of surface 1120 is near the sidewall 1122 and a second edge 1120B of surface 1120 is near the slurry injection channel 1110.

A clear fluid injection pipe 1124 which is in fluid communication with the flow distribution plates 64A is also illustrated. In the present example the clear fluid injection pipe 1124 corresponds to the longitudinal axis 42A of the system. Also, the tank 40A′, the slurry injection channel 1110 and the endcap 44A′ are all centered along the longitudinal axis 42A. However, such alignment is not necessary. The top of the endcap 1126 forms a horizontal plane which is perpendicular to the longitudinal axis 42A of the system and which is illustrated as a horizontal line 1126. The horizontal line 1126 defines the intersection of the sidewalls 1122 and the endcap 44A′.

The bottom surface 1120 of the tank 40A′ angles from the sidewall 1122 downward toward the slurry injection channel at an angle A. This forms a conical surface. The angle A is greater than zero degrees from the horizontal plane which is illustrated as a line 1126. The actual angle A may vary for different systems depending upon the size of the sand particles within the slurry and the type of fluid and chemicals within the tank. The angle A is greater than zero degrees but less than about forty-five degrees. In another example, the angle may be between about twenty degrees and about forty-five degrees. It is believed that an angle A less than twenty degrees may allow slurry particles to settle and thus not be washed into the slurry injection channel 1110 where they can be recirculated. However, as mentioned above the amount of settling may occur due to various factors of the particles in the fluid and the fluid itself. With the particles settling into the slurry injection channel 1110 as new slurry is received through the valve 82A, pipe 34 and slurry tank 30, the particles within the slurry injection tank are picked up in new slurry and mixed within the tank 40A′. An angle of about forty-five degrees may allow the slurry injection jet to be diffused resulting in low mixing turbulence and thus allowing slurry particles to lend toward settling. It is further believed that a range of about thirty-five to about forty degrees may be desirable. In operation, the valve 82A allows slurry to be injected into the tank 40A′ using low pressure. A jet of slurry forces the clear fluid toward the top of the tank 40A′. The bottom surface 1120 and the angle provided therein prevent the slurry particles from building up on the bottom surface of the tank.

Referring now to FIG. 11D, a bottom surface 1130 is hemispherical in shape. That is, the surface 1130 is curved downward from the side wall to the slurry injection channel 1110. The endcap 44A″ may have a hemispherical shape with the slurry injection channel 1110 at the bottom of the surface 1130. The pipe 60A is disposed within the slurry injection channel 1110 as described above in FIG. 11B. The hemispherical center is at point C. The tangent to the hemisphere is greater than a predetermined angle such as 20 degrees because the bottom of the circle has been removed at the slurry injection channel 1110. Of course various other curved shapes may be used as long as a diffuser is not formed.

Referring now generally to FIGS. 11E-J, in the previous examples, the top of the tank is flat and thus no potential for sand accumulation is present. This maximizes the tank volume for a given length. However, it has been found that a conical shape at the first end 46A of the tank may be suitable for diffusion of the clear water to minimize disturbance of the water/slurry interface 68A. A very dense slurry may benefit from a flat faced design as is illustrated above in various figures such as FIGS. 1A-1D, 1G, 1I, 1J, 1K and 11A. The flat upper surface design prevents the clear water jet from deeply penetrating the slurry volume. The flat surface also maximizes the usable tank volume. In the designs set forth below, a modified first end 46A may be used in low density slurry to minimize the disturbance of the slurry/water interface 68A caused by the jet of incoming clear water through the pipe 60A. The above examples largely eliminate diffusion of the incoming slurry to maximize formation of a jet moving upward in the center of the tank caused by the incoming slurry. The jet dissipates toward the top of the slurry volume at the first end of the tank 46A. At the point when the slurry volume is close to the top of the tank, the jet has entirely dissipated at the interface area 68A thus allowing a sharply defined interface to form. However, at the point of entry at the bottom of the tank through channel 1110, the jet is defined and causes a great amount of turbulence which minimizes the settling that may occur keeping the slurry density uniform. The length of the tank L₁ may be about seven or eight times the inside diameter W₁ of the tank 40A′. This allows the tank enough length for the incoming jet of slurry to dissipate before the slurry reaches the end wall 41.

Referring now to FIG. 11E, the first end 46A of a tank 40A has been modified. An external clear water pipe 1132 is used in place of pipe 60A and the diffuser 64A. Of course, in a two tank design both tanks 40A and 40B may be configured with the external clear water pipe 1132. In FIG. 11E the pipe 1132 has a diameter D2. The opening in a top surface 1142 of the tank 40A is also D2. The example illustrated in FIG. 11E is particularly suitable for high density slurry.

Referring now to FIG. 11F, a diffuser piece 1140 is attached within the first end 46A of the first tank 40A. The diffuser piece 1140 extends between the distribution plate 64A and a top surface 1142 of the tank 40A. In FIG. 11F the top surface 1142 is generally planer or perpendicular to the longitudinal direction of the tank. Angle B illustrated in the figure allows the surface 1144 to be conical in shape. Various angles for angle B may be used. In this example an angle B of about fifty degrees to about sixty degrees from the horizontal may be used. A flat horizontal surface 1146 may also be formed at the interface or top portion of the diffuser piece 1140. The diffuser piece 1140 has the flat surface or horizontal surface 1146 having a particular length. The length/diameter D1 of the surface 1146 may be about twice the diameter D₂ of the pipe 60A. Of course, different dimensions for the angle B and the distance D1 may be used. In fact D2 and D1 may be equivalent and thus eliminating the surface 1146. One example is of this is shown below in FIG. 11J.

Referring now to FIG. 11G, the diffuser piece 1140′ has been modified to fit into the tank 40 with a hemispheric end wall 1142′. The shape of the surface 1144 may be similar to that described above with respect to FIG. 11F, which is conical with a horizontal portion 1146. Likewise, the angle B may also be similar.

Referring now to FIG. 11H, the end wall 1142 and 1142′ illustrated in FIGS. 11F and 11G have been modified to form end walls 1150 and 1152. The end wall 1150 and 1152 may be disposed at the angle B. In a sense, the walls 1150 and 115 may act functionally as a diffuser.

Referring now to FIG. 11I, the end wall of the tank 40A′ is formed in a similar manner to that of 11H with the exception of an additional wall 1154. The wall 1150 and 1152 angle in a similar manner to that set forth above with respect to FIG. 11E in that the interior portions of the tank or the interior portions of the walls 1150 and 1152 are disposed at an angle B to form an integrated diffuser piece. The walls 1150 and 1152 are one continuous wall that forms a conical surface. In FIG. 11H the third wall 1154 is horizontal and may have a similar width D₁ which is about two times the width of the pipe D₂, in the present example.

Referring now to FIG. 11J, the tank 40A the diffuser piece 1140 includes a nozzle 1156. The nozzle expands from the diameter of the pipe D1 to the diameter D3 at the lower surface of the diffuser piece 1140. The angle B relative to horizontal may also vary as described above. The diameter D3 may be twice the diameter D1 to obtain the diffusing effect. The diffuser 1156 lowers the exit velocity of the clear fluid entering the tank 40A. The configuration of FIG. 11J is suitable for low density slurry.

The external pipe 1132 illustrated above may be substituted into the embodiments like FIGS. 1A-1K with the internal pipe 60A/60B while removing the flow distribution plates.

The embodiments shown in FIGS. 11F, 11G, 11H, 11I and 11J are particularly suitable when the unit is handling a low density slurry. The conical shape top end of the tank allows the diffusion of the incoming clear water flow.

Those skilled in the art can now appreciate from the foregoing description that the broad teachings of the disclosure can be implemented in a variety of forms. Therefore, while this disclosure includes particular examples, the true scope of the disclosure should not be so limited since other modifications will become apparent to the skilled practitioner upon a study of the drawings, the specification and the following claims. 

What is claimed is:
 1. A slurry injection system comprising: a low pressure clear fluid manifold; a high pressure clear fluid manifold; a plurality of clear fluid pumps receiving low pressure clear fluid from the low pressure clear fluid manifold, pressurizing the low pressure clear fluid into high pressure clear fluid and communicating the high pressure clear fluid into the high pressure clear fluid manifold; a blender unit having low pressure slurry therein comprising an outlet communicating the low pressure slurry therethrough; a sensor system coupled to the outlet generating a flow rate signal of the low pressure slurry and a density signal corresponding to a density of the low pressure slurry; a mixer in fluid communication with the high pressure clear fluid manifold and a slurry pressurizer; said slurry pressurizer in fluid communication with the high pressure clear fluid manifold through a bypass pump, the mixer, the blender unit and the low pressure clear fluid manifold, said slurry pressurizer forming high pressure slurry by pressurizing the low pressure slurry from the blender unit using high pressure clear fluid from the high pressure clear fluid manifold and the bypass pump, said slurry pressurizer communicating high pressure slurry to the mixer and communicating low pressure fluid to the low pressure clear fluid manifold; said mixer mixing the high pressure slurry and high pressure clear fluid from the high pressure clear fluid manifold to form a mixture that is communicated to a slurry injection site; and a controller coupled to the bypass pump and the sensor system, said controller controlling an operation of the bypass pump in response to the flow rate signal and the density signal to control a density of high pressure slurry.
 2. The slurry injection system as recited in claim 1 wherein a speed of the bypass pump is changed to obtain a predetermined density of the mixture.
 3. The slurry injection system as recited in claim 1 further comprising a slurry pressurizer bypass valve selectively coupling the outlet to the low pressure clear fluid manifold, said controller controlling the slurry pressurizer bypass valve to increase a concentration of the mixture communicated to the slurry injection site.
 4. The slurry injection system as recited in claim 1 further comprising a slurry pressurizer bypass valve selectively coupling the outlet to the low pressure clear fluid manifold, said controller monitoring the slurry pressurizer and controlling the slurry pressurizer bypass valve when a failure of the slurry pressurizer is detected in response to monitoring.
 5. The slurry injection system as recited in claim 4 further comprising a first isolation valve disposed between the high pressure clear fluid manifold and the bypass pump and a second isolation valve disposed between a high pressure slurry outlet of the slurry pressurizer and the injection site, wherein the controller controls the first isolation valve and the second isolation valve in response to the failure.
 6. The slurry injection system as recited in claim 5 wherein the controller controls relieving pressure in the slurry injection system after the failure.
 7. The slurry injection system as recited in claim 1 wherein said controller controls the bypass pump and the blender unit in response to an emergency.
 8. The slurry injection system as recited in claim 7 wherein the controller controls relieving pressure in the slurry unit in response to the emergency.
 9. The slurry injection system as recited in claim 1 further comprising a separator fluidically coupling the slurry pressurizer and the low pressure clear fluid manifold, said separator communicating slurry and clear fluid to the blender unit and low pressure clear fluid to the low pressure clear fluid manifold.
 10. A method of operating a slurry injection system comprising a low pressure clear fluid manifold, a high pressure clear fluid manifold, a plurality of clear fluid pumps, a blender unit having an outlet, a mixer, a bypass pump and a slurry pressurizer comprising: receiving low pressure clear fluid from the low pressure clear fluid manifold at the plurality of clear fluid pumps; pressurizing the low pressure clear fluid into high pressure clear fluid at the plurality of clear fluid pumps; communicating the high pressure clear fluid into the high pressure clear fluid manifold from the plurality of clear fluid pumps; communicating high pressure clear fluid from the high pressure clear fluid manifold to the mixer; communicating the high pressure clear fluid from the high pressure clear fluid manifold to the slurry pressurizer using a bypass pump; pressurizing, by the slurry pressurizer, low pressure slurry from the blender unit using high pressure clear fluid from the high pressure clear fluid manifold to form high pressure slurry; communicating low pressure fluid from the slurry pressurizer to the low pressure clear fluid manifold; blending, at a mixer, the high pressure slurry with high pressure clear fluid to form a slurry mixture; and communicating the mixture to a slurry injection site.
 11. The method of claim 10 wherein controlling the bypass pump comprises controlling a speed of the bypass pump.
 12. The method of claim 10 further comprising selectively controlling a slurry pressurizer bypass valve to selectively couple the outlet of the blender unit to the low pressure clear fluid manifold to increase a concentration of the mixture communicated to the slurry injection site.
 13. The method of claim 12 further comprising monitoring the slurry pressurizer and controlling the slurry pressurizer bypass valve when a failure of the slurry pressurizer is detected in response to monitoring.
 14. The method of claim 13 further comprising controlling a first isolation valve disposed between the high pressure clear fluid manifold and the slurry pressurizer and a second isolation valve disposed between a high pressure slurry outlet of the slurry pressurizer and the injection site in response to the failure.
 15. The method of claim 14 further comprising relieving pressure in the slurry injection system in response to the failure.
 16. The method of claim 10 further comprising controlling the bypass pump and blender unit in response to an emergency.
 17. The method of claim 16 further comprising relieving pressure in the slurry injection system in response to the emergency.
 18. A slurry injection system comprising: a low pressure clear fluid manifold; a high pressure clear fluid manifold; a plurality of clear fluid pumps receiving low pressure clear fluid from the low pressure clear fluid manifold and pressurizing the low pressure clear fluid into high pressure clear fluid and communicating the high pressure clear fluid into the high pressure clear fluid manifold; a blender unit having low pressure slurry therein; a mixer in fluid communication with the high pressure clear fluid manifold; and a slurry pressurizer in fluid communication with the high pressure clear fluid manifold, the mixer, the blender unit and the low pressure clear fluid manifold, said slurry pressurizer forming high pressure slurry by pressurizing the low pressure slurry from the blender unit using high pressure clear fluid from the high pressure clear fluid manifold, said slurry pressurizer communicating high pressure slurry to the mixer and communicating low pressure clear fluid to the low pressure clear fluid manifold and the low pressure clear fluid to the blender unit; said mixer mixing the high pressure slurry and high pressure clear fluid from the high pressure clear fluid manifold to form a mixture that is communicated to a slurry injection site.
 19. The slurry injection system as recited in claim 18 further comprising a separator fluidically coupling the slurry pressurizer and the low pressure clear fluid manifold, said separator communicating slurry and clear fluid to the blender unit and low pressure clear fluid to the low pressure clear fluid manifold.
 20. The slurry injection system as recited in claim 18 further comprising isolation valves operated adjacent the slurry pressurizer operating in response to a failure or an emergency. 